JP3966782B2 - Heat-shrinkable film and method for producing the same - Google Patents
Heat-shrinkable film and method for producing the same Download PDFInfo
- Publication number
- JP3966782B2 JP3966782B2 JP2002209654A JP2002209654A JP3966782B2 JP 3966782 B2 JP3966782 B2 JP 3966782B2 JP 2002209654 A JP2002209654 A JP 2002209654A JP 2002209654 A JP2002209654 A JP 2002209654A JP 3966782 B2 JP3966782 B2 JP 3966782B2
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- Prior art keywords
- film
- heat
- polyamide
- resin
- shrinkable film
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- 229920006257 Heat-shrinkable film Polymers 0.000 title claims description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 229920002647 polyamide Polymers 0.000 claims description 28
- 239000011347 resin Substances 0.000 claims description 27
- 229920005989 resin Polymers 0.000 claims description 27
- 229920001971 elastomer Polymers 0.000 claims description 18
- 239000000806 elastomer Substances 0.000 claims description 18
- 238000002844 melting Methods 0.000 claims description 8
- 230000008018 melting Effects 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000000034 method Methods 0.000 description 28
- 238000010438 heat treatment Methods 0.000 description 14
- 229920006300 shrink film Polymers 0.000 description 14
- 238000011156 evaluation Methods 0.000 description 12
- 239000005022 packaging material Substances 0.000 description 9
- 239000004952 Polyamide Substances 0.000 description 7
- -1 polyhexamethylene sebacamide Polymers 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 239000000314 lubricant Substances 0.000 description 6
- 229920006122 polyamide resin Polymers 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000005003 food packaging material Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000004806 packaging method and process Methods 0.000 description 4
- GVNWZKBFMFUVNX-UHFFFAOYSA-N Adipamide Chemical compound NC(=O)CCCCC(N)=O GVNWZKBFMFUVNX-UHFFFAOYSA-N 0.000 description 3
- 239000004721 Polyphenylene oxide Substances 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 238000005266 casting Methods 0.000 description 3
- 238000009998 heat setting Methods 0.000 description 3
- 229920000570 polyether Polymers 0.000 description 3
- 235000020991 processed meat Nutrition 0.000 description 3
- 229920002292 Nylon 6 Polymers 0.000 description 2
- 229920000305 Nylon 6,10 Polymers 0.000 description 2
- 229920002302 Nylon 6,6 Polymers 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- TVIDDXQYHWJXFK-UHFFFAOYSA-N dodecanedioic acid Chemical compound OC(=O)CCCCCCCCCCC(O)=O TVIDDXQYHWJXFK-UHFFFAOYSA-N 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 239000010954 inorganic particle Substances 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- CYIDZMCFTVVTJO-UHFFFAOYSA-N pyromellitic acid Chemical compound OC(=O)C1=CC(C(O)=O)=C(C(O)=O)C=C1C(O)=O CYIDZMCFTVVTJO-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000013580 sausages Nutrition 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 229930185605 Bisphenol Natural products 0.000 description 1
- 101000576320 Homo sapiens Max-binding protein MNT Proteins 0.000 description 1
- 229920000571 Nylon 11 Polymers 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 229920003189 Nylon 4,6 Polymers 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 1
- 229920006121 Polyxylylene adipamide Polymers 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- ORLQHILJRHBSAY-UHFFFAOYSA-N [1-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1(CO)CCCCC1 ORLQHILJRHBSAY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000003851 corona treatment Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 229940117969 neopentyl glycol Drugs 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 229920000052 poly(p-xylylene) Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000005033 polyvinylidene chloride Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、熱収縮性フィルム(以下、シュリンクフィルムともいう)およびその製造方法に関する。更に詳しくは水物食品、ハム、ソーセージ等の加工食肉製品等の収縮包装用に好適な、収縮性と滑り性に優れた包装用シュリンクフィルムおよびその製造方法に関する。
【0002】
【従来の技術】
加熱により大きな寸法変化を生じるいわゆる熱収縮性(以下シュリンクともいう)フィルムは、その特性を生かして包装材料として使用されている。熱収縮性フィルムの構成素材として、従来ポリ塩化ビニル、ポリ塩化ビニリデン、ポリオレフィン、ポリアミド等およびこれらの共重合物等が知られている。なかでも、ポリアミド樹脂は本来優れた機械的、化学的および光学的性質を備えているため、これに適当な熱収縮性を加味したシュリンクフィルムは、シュリンク包装材料として要求される多くの性能を満足することから、水物食品、ハム、ソーセージ等の食肉加工製品をはじめとする液体および重包装材料として広く利用されている。
【0003】
二軸延伸フィルムの製造工程において、一般に、延伸工程後に主構成素材樹脂の融点付近で熱処理を施し、結晶化を促進して配向を固定するいわゆる熱セット工程が設けられている。シュリンクフィルムの製造工程においては、この熱セットの条件が緩和されている。即ち、延伸終了後のフィルムは比較的低温で熱処理される。したがって、シュリンクフィルム内部には一定の構造歪みが残存するため、フィルムには収縮特性が付与されることになる。ポリアミド系シュリンクフィルムに関しても同様にして収縮特性が付与される。
【0004】
一方、プラスチックフィルムを包装材料として利用する為には、その表面の滑り性が良好であることが必要である。一般に、無機粒子や低分子有機化合物をいわゆる滑剤としてフィルムに添加し、フィルム表面に易滑性を付与する技術は公知であり、広く実施されている。特に有機系滑剤は動摩擦の緩和に威力を発揮し、包装体への内容物の充填性向上に有効である。
【0005】
有機滑剤がその効果を充分に発揮するためには、フィルム表面への該成分の移行が速やかにかつ確実になされなければならない。いわゆる有機滑剤のブリードアウトと呼ばれる表面移行は、滑剤成分を予め原料樹脂と充分に混練シート化し二軸延伸した後、上述した熱セット工程において、専ら高温度下で熱処理を施すことにより進行する。
【0006】
つまり、従来のシュリンクフィルムでは必須特性の熱収縮性を付与するために、熱処理温度を低く設定する必要があるため、必然的に有機滑剤の表面移行は促進されることなく、一般に滑り性は十分に発現しない。特に該フィルムを包装体として使用し、印刷・ラミネート加工や食品充填する際、しばしば工程不良の原因となる。
【0007】
ケイ酸塩をはじめとする無機成分よりなる微粒子を多量に添加することにより、低熱処理条件下でも一定の滑り性は得られるが、この方法では著しい曇度上昇や表面光沢の欠損などフィルム外観不良を併発し、食品包材としての商品価値を著しく損なうことになる。また無機粒子の過剰な添加は、原料樹脂の溶融押出工程における押出機内のスクリュー・バレル等の摩耗や、異物除去用の濾過フィルター目詰まりによる寿命短縮など、製造工程上看過することの出来ない問題の原因となり得るなど、一般に好ましい方法とはいい難い。
【0008】
以上のように、ポリアミド系シュリンクフィルムを食品包装材料として使用する際、その特性として欠かすことの出来ない熱収縮性と滑り性を同時に付与し並立させることは困難であり、昨今の食品包材に対する厳しい品質水準に鑑みて、その要求に応えられないことがしばしばある。
【0009】
【発明が解決しようとする課題】
本発明は、シュリンク包装材料として欠かせない特性である熱収縮性を維持し、かつ滑り性に優れたシュリンクフィルムを提供しようというものである。
【0010】
【課題を解決するための手段】
本発明者は、ポリアミド樹脂組成物よりなるフィルムの製造工程において、その構成成分としてのポリアミド系エラストマー樹脂の挙動に着目し、ポリアミド樹脂への配合濃度および二軸延伸終了後の熱処理温度を適切に設定することにより、熱収縮性を損なうことなく優れた滑り性を有するポリアミドフィルムを製造することが出来ることを見出し、本発明に到達したものである。
【0011】
すなわち、本発明の要旨は、次の通りである。
ポリアミド系樹脂(a)とポリアミド系エラストマー樹脂(b)とからなるフィルムであって、(a)の含有量が80〜97質量%、(b)の含有量が3〜20質量%であり、動摩擦係数が0.8以下であり、かつ80℃熱水中で30分処理した際の収縮率が15〜40%であることを特徴とする滑り性に優れた熱収縮性フィルムである。
【0012】
【発明の実施の形態】
以下、本発明を詳細に説明する。
本発明の熱収縮性フィルムは、ポリアミド系樹脂(a)とポリアミド系エラストマー樹脂(b)とから構成される。ポリアミド系樹脂(a)として、例えばポリ−ε−カプラミド(ナイロン6)、ポリヘキサメチレンアジパミド(ナイロン66)、ポリヘキサメチレンセバカミド(ナイロン610)、ポリウンデカミド(ナイロン11)、ポリラウラミド(ナイロン12)、ポリテトラメチレンアジパミド(ナイロン46)、ポリメタキシリレンアジパミド(MXD6)、ポリメタキシリレンサバカミド、ポリメタキシリレンスペラミド、ポリパラキシリレンアジパミドおよびこれらの混合物、共重合体等が例示できる。以上のポリアミド系樹脂を本発明のフィルムに適用すると優れた効果が得られ、機械的性質、耐熱性および透明性等包装材料として好適な特性を有するフィルムを得ることが出来る。
【0013】
ポリアミド系エラストマー樹脂とは、ポリアミド成分をハードセグメントとし、これにポリエーテルもしくはポリエステル成分または両成分をソフトセグメントとして、両者をブロック共重合して得られるブロック共重合体である。
【0014】
ポリアミド成分としては上述したポリアミド樹脂と同様の成分を任意に例示することができる。ソフトセグメント成分であるポリエーテルとしては、ポリエチレングリコール、ポリプロピレングリコール、ポリテトラメチレングリコール等のいわゆるポリエーテルグリコール、およびこれらの共重合体が例示できる。またポリエステルとしては、テレフタル酸、フタル酸、イソフタル酸、トリメリット酸、ピロメリット酸、アジピン酸、セバチン酸、コハク酸、ドデカン二酸などの多価カルボン酸成分と、エチレングリコール、プロピレングリコール、1,4−ブタンジオール、1,6−ヘキサンジオール、ネオペンチルグリコール、シクロヘキサンジメタノール、ビスフェノールなどのジオール成分との重縮合物、反応物が挙げられ、アクリル樹脂、エポキシ樹脂などによる変性物も含まれる。
【0015】
本発明の熱収縮性フィルムにおいて、フィルム中のポリアミド系樹脂(a)の含有量は80〜97質量%であり、ポリアミド系エラストマー樹脂(b)の含有量は3〜20質量%であることが必要である。(b)の含有量が3質量%より低いと所定の滑り性が得られない。また20質量%より高く設定すると、逆に滑り性が過剰となり、フィルムのスリット工程におけるフィルム巻取の際に発生する、いわゆる巻きずれにより製品形態が崩れることがあり、またフィルム白化による外観不良も問題となるなどその製品価値を損なうことになる。一方操業上もシート化時のダイスウェルによる製膜不良や幅方向のフィルム厚み不良が顕著となるなど経済的にも好ましくない。
【0016】
本発明のフィルムは、動摩擦係数が0.8以下であることが必要がある。フィルムの動摩擦挙動は、食品をはじめとする内容物を連続充填する際、充填装置にかけられた包材が円滑に装置内を流れ充填工程に供されるために欠くことの出来ない特性であり、特に昨今の高速充填において極めて重要な特性とされる。動摩擦係数が0.8以下であれば、充填装置内でのシワ発生や装置パーツへの引っかかり等の問題は発生しにくい。
【0017】
本発明のフィルムは、80℃熱水中で30分間処理した際の収縮率が15〜40%の範囲にあることが必要がある。該収縮率が15%未満の場合、シュリンク包装材料として適当な収縮性を確保することが出来ず、包装内容物との密着が悪くシュリンク包装の特徴を発揮することが出来ない。40%を超えると、その過大なフィルム収縮により包装形態が崩れ、内容物の破損や包装材の破袋が発生し、食品包材としての機能や商品外観を著しく損なうことになる。
【0018】
本発明の熱収縮フィルムの製造方法としては、公知の任意の方法を採用することが出来る。例えば、混合した原料を押出機で加熱溶融した後、TダイやIダイ等のダイより未延伸シートを押出し、これをエアーナイフキャスト法、静電印加キャスト法等の公知のキャスティング法で回転する冷却ドラム上に密着させて急冷製膜する。
【0019】
次に、得られた未延伸シートをフィルムの進行方向(以下MD方向)および巾方向(以下TD方向)に共に2.5倍以上延伸した後、熱処理して配向結晶化させる。フィルムの延伸方法としてはフラット式逐次二軸延伸法、フラット式同時二軸延伸法等の方法を適用することが可能である。延伸倍率が2.5倍以下の場合配向結晶化が不十分となり耐衝撃性等の機械的強度が得られない。
【0020】
本発明において、二軸延伸終了後の熱処理工程は、ポリアミド系エラストマー樹脂(b)の融点以上、170℃以下の熱処理温度で実施することが好ましい。熱処理温度が樹脂(b)の融点以下の場合、フィルムの滑り性が得られないことがあり、また収縮も過大となり、包装形態が崩れ内容物の破損が起こるなど、食品包装材料としての用をなさなくなることがある。一方、熱処理温度が170℃を超えると、配向結晶化が過促進されることにより、逆に熱収縮性は低下しシュリンク包装材料としての特徴が失われることになり、その製品価値を著しく損なうことになる。
【0021】
本発明のフィルムを構成するポリアミド樹脂もしくは本発明により提供されるフィルムには、本発明の効果を消失させない範囲において、必要に応じて帯電防止剤、着色防止剤、無機フィラー等の各種添加剤を配合することも可能である。
【0022】
本発明により提供されるポリアミドフィルムは、その表面にコロナ処理をはじめとする表面活性処理を施したり、印刷、各種機能コーティング、ラミネート等を行うことにより諸性能を付加し、その利用価値をさらに向上させることも可能である。
【0023】
このようにして得られたシュリンクフィルムは、適当な熱収縮性と優れた滑り性を有し、包装用シュリンクフィルムとして好適である。
【0024】
【実施例】
次に、本発明を実施例により具体的に説明するが、本発明はこれらの実施例のみに限定されるものではない。なお、実施例および比較例に用いた測定法および評価法は次の通りである。
【0025】
(1)熱水収縮率
巾10mm、長さ100mmのフィルム片を80℃熱水中に30分間浸漬し、処理前後の寸法変化を測定して、原長に対する百分率で求めた。
【0026】
(2)動摩擦係数
JISK7125記載の手順により動摩擦係数を測定したが、測定雰囲気温度は20℃、同相対湿度は65%とした。なお、測定面は試験片、滑り片ともに測定対象フィルム片である。
【0027】
実施例1
ポリ−ε−カプラミド(ナイロン6、相対粘度3.0(25℃、95質量%硫酸中))93質量%と、ポリアミド系エラストマー樹脂<A>(アトフィナ社製ぺバックス2533、融点134℃)7質量%とを240℃で混合溶融し、Tダイを用いてシート状に押出した後、エアーナイフキャスト方式により25℃の回転ドラムに密着させて急冷し、厚さ150μmの未延伸シートを得た。
続いてこの未延伸フィルムを、50〜70℃に加熱した金属ロール上で長手方向に3.0倍に延伸して一軸延伸フィルムを得、更にテンター式横延伸機で巾方向に90℃で3.3倍延伸して二軸延伸フィルムを得た。
次いで、二軸延伸フィルムを熱処理温度150℃で10秒間熱処理し、冷却後巻取り、厚さ15μmの熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0028】
実施例2
未延伸シートをテンター式同時二軸延伸機で90℃で長手方向に3.0倍、横方向に3.3倍同時二軸延伸すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0029】
実施例3〜4
実施例1で使用したポリアミド系エラストマー樹脂<A>の含有量を表1記載の量に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0030】
実施例5
ポリアミド系エラストマー樹脂<A>を別のエラストマー樹脂<B>(アトフィナ社製ぺバックスMX1205、融点147℃)に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0031】
実施例6
ポリアミド系エラストマー樹脂<A>を別のエラストマー樹脂<C>(ダイセル工業社製ダイアミドE40、融点146℃)に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0032】
実施例7
熱処理温度を165℃に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0033】
比較例1
ポリアミド系エラストマー樹脂<A>を添加しないこと以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0034】
比較例2〜3
実施例1で使用したポリアミド系エラストマー樹脂<A>の含有量を表1記載の量に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0035】
比較例4
熱処理温度を120℃に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0036】
比較例5
熱処理温度を200℃に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0037】
比較例6
ポリアミド系エラストマー樹脂<A>を別のエラストマー樹脂<D>(アトフィナ社製ぺバックス7033、融点172℃)に変更すること以外は、実施例1と同様の手順で熱収縮性フィルムを得た。得られたフィルムの評価結果を表1に示す。
【0038】
【表1】
【0039】
【発明の効果】
本発明によれば、シュリンク包装材料として適当な熱水収縮率を有すると共に、包装材料として適当な表面易滑性を有する熱収縮性ポリアミドフィルムを提供することが可能である。したがって本発明のシュリンクフィルムは、水物食品、食肉加工品をはじめとする収縮包装用途において、その利用価値は極めて高い。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a heat-shrinkable film (hereinafter also referred to as a shrink film) and a method for producing the same. More particularly, the present invention relates to a shrink film and a shrink film excellent in shrinkability and slipperiness suitable for shrinkage packaging of processed meat products such as marine foods, ham and sausage, and a method for producing the same.
[0002]
[Prior art]
A so-called heat-shrinkable (hereinafter also referred to as shrink) film that causes a large dimensional change by heating is used as a packaging material taking advantage of its characteristics. Conventionally, polyvinyl chloride, polyvinylidene chloride, polyolefin, polyamide, and their copolymers are known as constituent materials for heat-shrinkable films. Among them, polyamide resin inherently has excellent mechanical, chemical and optical properties, so a shrink film with appropriate heat shrinkability satisfies many performance requirements for shrink packaging materials. Therefore, it is widely used as liquid and heavy packaging materials including processed meat products such as marine foods, hams and sausages.
[0003]
In the manufacturing process of a biaxially stretched film, generally, a so-called heat setting process is performed in which heat treatment is performed near the melting point of the main constituent resin after the stretching process to promote crystallization and fix the orientation. In the manufacturing process of the shrink film, this heat setting condition is relaxed. That is, the film after stretching is heat-treated at a relatively low temperature. Therefore, since a certain structural strain remains in the shrink film, the film is given shrinkage characteristics. Similarly, shrinkage characteristics are imparted to polyamide-based shrink films.
[0004]
On the other hand, in order to use a plastic film as a packaging material, it is necessary that the slipperiness of the surface is good. In general, a technique of adding inorganic particles or a low molecular weight organic compound as a so-called lubricant to a film to impart easy slipping to the film surface is known and widely practiced. In particular, organic lubricants are effective in reducing dynamic friction and are effective in improving the filling of the contents into the package.
[0005]
In order for the organic lubricant to fully exert its effect, the component must be quickly and reliably transferred to the film surface. Surface migration called so-called bleed-out of the organic lubricant proceeds by subjecting the lubricant component to a kneaded sheet with a raw material resin in advance and biaxially stretching, followed by heat treatment exclusively at a high temperature in the heat setting step described above.
[0006]
In other words, the conventional shrink film needs to be set at a low heat treatment temperature in order to provide the heat shrinkability that is an essential characteristic. Therefore, the surface migration of the organic lubricant is inevitably promoted, and the slipperiness is generally sufficient. Not expressed in In particular, when the film is used as a package and printing / laminating or filling food, it often causes a process failure.
[0007]
By adding a large amount of fine particles composed of inorganic components such as silicate, a certain level of slipperiness can be obtained even under low heat treatment conditions, but this method has a poor film appearance such as a significant increase in haze and loss of surface gloss. This will significantly impair the commercial value of the food packaging material. In addition, excessive addition of inorganic particles is a problem that cannot be overlooked in the manufacturing process, such as wear of screws and barrels in the extruder in the melt extrusion process of the raw resin, and shortening of the service life due to clogging of the filter for removing foreign matter. In general, it is difficult to say that it is a preferable method.
[0008]
As described above, when using a polyamide-based shrink film as a food packaging material, it is difficult to simultaneously provide heat shrinkability and slipperiness that are indispensable as properties, and it is difficult to make it parallel to the current food packaging materials. In view of strict quality standards, the demand is often not met.
[0009]
[Problems to be solved by the invention]
The present invention aims to provide a shrink film that maintains heat shrinkability, which is an indispensable characteristic for shrink wrapping materials, and is excellent in slipperiness.
[0010]
[Means for Solving the Problems]
The present inventor pays attention to the behavior of the polyamide-based elastomer resin as a component in the production process of the film comprising the polyamide resin composition, and appropriately sets the compounding concentration in the polyamide resin and the heat treatment temperature after the biaxial stretching is completed. By setting, it has been found that a polyamide film having excellent slipperiness can be produced without impairing heat shrinkability, and the present invention has been achieved.
[0011]
That is, the gist of the present invention is as follows.
A film comprising a polyamide-based resin (a) and a polyamide-based elastomer resin (b), wherein the content of (a) is 80 to 97% by mass, the content of (b) is 3 to 20% by mass, It is a heat-shrinkable film excellent in slipperiness, having a dynamic friction coefficient of 0.8 or less and a shrinkage rate of 15 to 40% when treated in hot water at 80 ° C. for 30 minutes.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail.
The heat-shrinkable film of the present invention is composed of a polyamide resin (a) and a polyamide elastomer resin (b). Examples of the polyamide-based resin (a) include poly-ε-capramide (nylon 6), polyhexamethylene adipamide (nylon 66), polyhexamethylene sebacamide (nylon 610), polyundecamide (nylon 11), polylauramide (nylon) 12), polytetramethylene adipamide (nylon 46), polymetaxylylene adipamide (MXD6), polymetaxylylene sacacamide, polymetaxylylene speramide, polyparaxylylene adipamide and mixtures thereof, A polymer etc. can be illustrated. When the above polyamide-based resin is applied to the film of the present invention, excellent effects can be obtained, and a film having properties suitable as a packaging material such as mechanical properties, heat resistance, and transparency can be obtained.
[0013]
The polyamide-based elastomer resin is a block copolymer obtained by block copolymerizing a polyamide component as a hard segment and a polyether or polyester component or both components as a soft segment.
[0014]
As a polyamide component, the component similar to the polyamide resin mentioned above can be illustrated arbitrarily. Examples of the polyether which is a soft segment component include so-called polyether glycols such as polyethylene glycol, polypropylene glycol and polytetramethylene glycol, and copolymers thereof. Polyesters include terephthalic acid, phthalic acid, isophthalic acid, trimellitic acid, pyromellitic acid, adipic acid, sebacic acid, succinic acid, dodecanedioic acid and other polycarboxylic acid components, ethylene glycol, propylene glycol, 1 , 4-butanediol, 1,6-hexanediol, neopentylglycol, cyclohexanedimethanol, bisphenol and other polycondensates and reactants are included, and modified products such as acrylic resins and epoxy resins are also included. .
[0015]
In the heat-shrinkable film of the present invention, the content of the polyamide-based resin (a) in the film is 80 to 97% by mass, and the content of the polyamide-based elastomer resin (b) is 3 to 20% by mass. is necessary. If the content of (b) is lower than 3% by mass, a predetermined slip property cannot be obtained. On the other hand, if it is set higher than 20% by mass, the slipping property becomes excessive, and the product form may be broken due to so-called winding deviation that occurs during film winding in the film slitting process. It will damage the product value such as problems. On the other hand, it is not economically preferable from the standpoint of operation, such as film formation failure due to die swell and sheet thickness failure in the width direction become remarkable.
[0016]
The film of the present invention needs to have a dynamic friction coefficient of 0.8 or less. The dynamic friction behavior of the film is an indispensable characteristic because the packaging material applied to the filling device smoothly flows through the device and is used for the filling process when continuously filling the contents including food. In particular, it is an extremely important characteristic in recent high-speed filling. If the dynamic friction coefficient is 0.8 or less, problems such as wrinkling in the filling device and catching on device parts are unlikely to occur.
[0017]
The film of the present invention needs to have a shrinkage ratio in the range of 15 to 40% when treated in hot water at 80 ° C. for 30 minutes. When the shrinkage rate is less than 15%, it is impossible to ensure appropriate shrinkage as a shrink wrapping material, and the adhesion with the package contents is poor and the characteristics of shrink wrapping cannot be exhibited. When it exceeds 40%, the packaging form collapses due to the excessive film shrinkage, the contents are damaged and the packaging material is broken, and the function as a food packaging material and the appearance of the product are remarkably impaired.
[0018]
Any known method can be adopted as a method for producing the heat-shrinkable film of the present invention. For example, after the mixed raw materials are heated and melted by an extruder, an unstretched sheet is extruded from a die such as a T die or an I die, and this is rotated by a known casting method such as an air knife casting method or an electrostatic application casting method. The film is rapidly cooled by being brought into close contact with the cooling drum.
[0019]
Next, the obtained unstretched sheet is stretched by 2.5 times or more in the traveling direction (hereinafter referred to as MD direction) and the width direction (hereinafter referred to as TD direction) of the film, and then heat-treated to cause oriented crystallization. As a method for stretching the film, it is possible to apply methods such as a flat sequential biaxial stretching method and a flat simultaneous biaxial stretching method. When the draw ratio is 2.5 or less, oriented crystallization is insufficient and mechanical strength such as impact resistance cannot be obtained.
[0020]
In the present invention, the heat treatment step after the end of biaxial stretching is preferably performed at a heat treatment temperature of not less than the melting point of the polyamide-based elastomer resin (b) and not more than 170 ° C. If the heat treatment temperature is lower than the melting point of the resin (b), the slipperiness of the film may not be obtained, the shrinkage will be excessive, the packaging form will collapse and the contents will be damaged, etc. It may disappear. On the other hand, when the heat treatment temperature exceeds 170 ° C., the orientation crystallization is excessively promoted, conversely, the heat shrinkability is lowered and the characteristics as a shrink wrapping material are lost, and the product value is significantly impaired. become.
[0021]
Various additives such as an antistatic agent, an anti-coloring agent and an inorganic filler are added to the polyamide resin constituting the film of the present invention or the film provided by the present invention, as long as the effects of the present invention are not lost. It is also possible to mix.
[0022]
The polyamide film provided by the present invention adds various performances by performing surface activation treatment such as corona treatment on the surface, printing, various functional coatings, laminating, etc., and further improving its utility value. It is also possible to make it.
[0023]
The shrink film thus obtained has appropriate heat shrinkage and excellent slipperiness and is suitable as a shrink film for packaging.
[0024]
【Example】
EXAMPLES Next, although an Example demonstrates this invention concretely, this invention is not limited only to these Examples. The measurement methods and evaluation methods used in the examples and comparative examples are as follows.
[0025]
(1) A film piece having a hot water shrinkage ratio of 10 mm and a length of 100 mm was immersed in hot water at 80 ° C. for 30 minutes, and the dimensional change before and after the treatment was measured to obtain the percentage of the original length.
[0026]
(2) Coefficient of dynamic friction The coefficient of dynamic friction was measured according to the procedure described in JISK7125. The measurement ambient temperature was 20 ° C. and the relative humidity was 65%. The measurement surface is a film piece to be measured for both the test piece and the sliding piece.
[0027]
Example 1
93% by mass of poly-ε-capramide (nylon 6, relative viscosity 3.0 (25 ° C., 95% by mass in sulfuric acid)) and polyamide-based elastomer resin <A> (Pebux 2533, manufactured by Atofina, melting point 134 ° C.) 7 After being mixed and melted at 240 ° C. and extruded into a sheet using a T-die, it was brought into close contact with a rotating drum at 25 ° C. by an air knife cast method and rapidly cooled to obtain an unstretched sheet having a thickness of 150 μm. .
Subsequently, this unstretched film was stretched 3.0 times in the longitudinal direction on a metal roll heated to 50 to 70 ° C. to obtain a uniaxially stretched film, and further 3 ° C. at 90 ° C. in the width direction. The film was stretched 3 times to obtain a biaxially stretched film.
Next, the biaxially stretched film was heat-treated at a heat treatment temperature of 150 ° C. for 10 seconds, wound after cooling, and a heat-shrinkable film having a thickness of 15 μm was obtained. The evaluation results of the obtained film are shown in Table 1.
[0028]
Example 2
Heat shrinkability in the same procedure as in Example 1 except that the unstretched sheet is stretched simultaneously at 90 ° C. by 3.0 times in the longitudinal direction and 3.3 times in the transverse direction at 90 ° C. A film was obtained. The evaluation results of the obtained film are shown in Table 1.
[0029]
Examples 3-4
A heat-shrinkable film was obtained in the same procedure as in Example 1, except that the content of the polyamide-based elastomer resin <A> used in Example 1 was changed to the amount shown in Table 1. The evaluation results of the obtained film are shown in Table 1.
[0030]
Example 5
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the polyamide-based elastomer resin <A> was changed to another elastomer resin <B> (Pebux MX1205 manufactured by Atofina, melting point 147 ° C.). The evaluation results of the obtained film are shown in Table 1.
[0031]
Example 6
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the polyamide-based elastomer resin <A> was changed to another elastomer resin <C> (Daicel E40 manufactured by Daicel Industries, Ltd., melting point 146 ° C.). The evaluation results of the obtained film are shown in Table 1.
[0032]
Example 7
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the heat treatment temperature was changed to 165 ° C. The evaluation results of the obtained film are shown in Table 1.
[0033]
Comparative Example 1
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the polyamide-based elastomer resin <A> was not added. The evaluation results of the obtained film are shown in Table 1.
[0034]
Comparative Examples 2-3
A heat-shrinkable film was obtained in the same procedure as in Example 1, except that the content of the polyamide-based elastomer resin <A> used in Example 1 was changed to the amount shown in Table 1. The evaluation results of the obtained film are shown in Table 1.
[0035]
Comparative Example 4
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the heat treatment temperature was changed to 120 ° C. The evaluation results of the obtained film are shown in Table 1.
[0036]
Comparative Example 5
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the heat treatment temperature was changed to 200 ° C. The evaluation results of the obtained film are shown in Table 1.
[0037]
Comparative Example 6
A heat-shrinkable film was obtained in the same procedure as in Example 1 except that the polyamide-based elastomer resin <A> was changed to another elastomer resin <D> (Pebux 7033 manufactured by Atofina, melting point 172 ° C.). The evaluation results of the obtained film are shown in Table 1.
[0038]
[Table 1]
[0039]
【The invention's effect】
ADVANTAGE OF THE INVENTION According to this invention, it is possible to provide the heat-shrinkable polyamide film which has a suitable hot-water shrinkage rate as a shrink packaging material, and has a suitable surface slipperiness as a packaging material. Therefore, the shrink film of the present invention has extremely high utility value in shrink wrapping applications including marine foods and processed meat products.
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