JPH0459333A - Polyester shrink film for label - Google Patents
Polyester shrink film for labelInfo
- Publication number
- JPH0459333A JPH0459333A JP17219190A JP17219190A JPH0459333A JP H0459333 A JPH0459333 A JP H0459333A JP 17219190 A JP17219190 A JP 17219190A JP 17219190 A JP17219190 A JP 17219190A JP H0459333 A JPH0459333 A JP H0459333A
- Authority
- JP
- Japan
- Prior art keywords
- film
- shrinkage
- dicarboxylic acid
- acid component
- longitudinal direction
- 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.)
- Pending
Links
- 229920000728 polyester Polymers 0.000 title claims abstract description 18
- 229920006300 shrink film Polymers 0.000 title claims description 11
- 238000000034 method Methods 0.000 abstract description 16
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 abstract description 11
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 abstract description 8
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 abstract description 8
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 abstract description 6
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 abstract description 6
- 125000001931 aliphatic group Chemical group 0.000 abstract description 4
- 150000002009 diols Chemical class 0.000 abstract description 4
- 239000001361 adipic acid Substances 0.000 abstract description 3
- 235000011037 adipic acid Nutrition 0.000 abstract description 3
- 230000009477 glass transition Effects 0.000 abstract description 3
- 229920001577 copolymer Polymers 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 description 9
- 238000001816 cooling Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000010419 fine particle Substances 0.000 description 4
- -1 polyethylene terephthalate Polymers 0.000 description 4
- 229920001634 Copolyester Polymers 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 230000004927 fusion Effects 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 description 3
- 239000005020 polyethylene terephthalate Substances 0.000 description 3
- 229920005992 thermoplastic resin Polymers 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000008602 contraction Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- TVIDDXQYHWJXFK-UHFFFAOYSA-N dodecanedioic acid Chemical compound OC(=O)CCCCCCCCCCC(O)=O TVIDDXQYHWJXFK-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 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
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical compound [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 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
- 229920000642 polymer Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000005995 Aluminium silicate Substances 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001339 alkali metal compounds Chemical class 0.000 description 1
- 150000001341 alkaline earth metal compounds Chemical class 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- AAEHPKIXIIACPQ-UHFFFAOYSA-L calcium;terephthalate Chemical compound [Ca+2].[O-]C(=O)C1=CC=C(C([O-])=O)C=C1 AAEHPKIXIIACPQ-UHFFFAOYSA-L 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000003851 corona treatment Methods 0.000 description 1
- 229920006037 cross link polymer Polymers 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 229920006267 polyester film Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 238000003466 welding 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)
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、優れた収縮特性および強度を有するラベル用
ポリエステル系収縮フィルムに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a polyester shrink film for labels having excellent shrink properties and strength.
〔従来の技術および発明が解決しようとする課題〕近年
、ポリエステル系のラベル用収縮フィルムは、廃棄時の
燃焼性の問題、あるいはPETボトルへ装着後の回収性
の問題を解消できるフィルムとして、注目を集めている
。[Prior art and problems to be solved by the invention] In recent years, polyester-based shrink film for labels has attracted attention as a film that can solve the problems of flammability during disposal and recyclability after being attached to PET bottles. are collecting.
ラベル用収縮フィルムにおいて特に必要とされる特性の
1つとして、一方向に大きい収縮性を有するとともに、
これと直交方向にはほとんど収縮しないことが挙げられ
る。しかしながら、一方向のみに大きい収縮性を有する
フィルムを得るために、例えば、単純にフィルムの横方
向にのみ強く配向させると、フィルムの縦方向について
は、引裂けやすく、強度も弱くなってしまう。One of the properties particularly required for shrink film for labels is to have high shrinkability in one direction,
Another reason is that there is almost no contraction in the direction perpendicular to this. However, in order to obtain a film that has high shrinkability in only one direction, for example, if the film is simply strongly oriented only in the transverse direction, the film will be easily torn and its strength will be weakened in the longitudinal direction.
ラベル用フィルムは、印刷、製袋および裁断加工を経て
製造されるが、縦方向に引裂けやすく、強度の弱いフィ
ルムを用いると、上記加工工程において、フィルムの破
断が頻発し、生産性が非常に低下する。Label films are manufactured through printing, bag making, and cutting processes, but if a film with low strength is used because it easily tears in the vertical direction, the film will frequently break during the above processing steps, resulting in extremely low productivity. decreases to
従って、一方向に高い収縮性を持ち、かつ、該方向と直
交する方向に引裂は難く、強度の優れたラベル用収縮フ
ィルムが切望されていた。Therefore, a shrink film for labels that has high shrinkability in one direction, is difficult to tear in a direction perpendicular to that direction, and has excellent strength has been desired.
本発明者らは、上記課題に鑑み、鋭意検討した結果、あ
る特定の収縮特性および強度を有するポリエステルフィ
ルムがラベル用収縮フィルムとして、極めて有用である
ことを見いだし、本発明を完成するに至った。In view of the above-mentioned problems, the present inventors have conducted extensive studies and found that a polyester film having certain shrinkage characteristics and strength is extremely useful as a shrink film for labels, and have completed the present invention. .
すなわち本発明の要旨は、100℃エアーオープン中で
5分間処理後のフィルムの収縮率が横方向において40
%以上であり、縦方向において20%以下であり、かつ
、フィルムの縦方向の破断伸度が250%以上であるこ
とを特徴とするラベル用ポリエステル系収縮フィルムに
存する。That is, the gist of the present invention is that the shrinkage rate of the film after being treated in an air open environment at 100°C for 5 minutes is 40% in the transverse direction.
% or more, and 20% or less in the machine direction, and the elongation at break in the machine direction of the film is 250% or more.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明のポリエステルにおいては、ジカルボン酸成分と
してテレフタル酸、ジオール成分としてエチレングリコ
ールを主成分とする共重合ポリエステルが好ましく用い
られ、該共重合成分としてはジカルボン酸成分としてイ
ソフタル酸、フタル酸、アジピン酸、セバシン酸、1,
10−デカンジカルボン酸、ジオール成分としてネオペ
ンチルグリコール、ジエチレングリコール、ポリアルキ
レングリコール、1,4−シクロヘキサンジメタツール
を用いた共重合ポリエステルが、工業的に安価に入手で
き、かつ、収縮特性も良好で好ましい。In the polyester of the present invention, a copolymerized polyester mainly containing terephthalic acid as the dicarboxylic acid component and ethylene glycol as the diol component is preferably used, and the copolymerized polyester includes isophthalic acid, phthalic acid, adipic acid as the dicarboxylic acid component. , sebacic acid, 1,
Copolyesters using 10-decanedicarboxylic acid, neopentyl glycol, diethylene glycol, polyalkylene glycol, and 1,4-cyclohexane dimetatool as diol components are industrially available at low cost and have good shrinkage properties. preferable.
本発明で用いられる共重合ポリエステルにおいて、共重
合成分の一つとしてジカルボン酸成分を用いることは、
フィルムの収縮応力を減少させる点で好ましい。特に、
アジピン酸、セバシン酸、1.10−デカンジカルボン
酸等の脂肪族ジカルボン酸成分が、フィルムのガラス転
移温度と結晶性を低下させ、主収縮方向の最大収縮応力
を大きく低下させることができ好ましい。本発明の共重
合ポリエステルにおいて、上記脂肪族ジカルボン酸成分
の含有量としては、好ましくは1〜25mof%、更に
好ましくは2〜20mo1%である。In the copolymerized polyester used in the present invention, the use of a dicarboxylic acid component as one of the copolymerization components is as follows:
This is preferable in that it reduces the shrinkage stress of the film. especially,
Aliphatic dicarboxylic acid components such as adipic acid, sebacic acid, and 1,10-decanedicarboxylic acid are preferred because they can lower the glass transition temperature and crystallinity of the film and greatly reduce the maximum shrinkage stress in the main shrinkage direction. In the copolymerized polyester of the present invention, the content of the aliphatic dicarboxylic acid component is preferably 1 to 25 mof%, more preferably 2 to 20 mo1%.
かかる含有量が25mof%を越えるフィルムではTg
の低下が著しく、フィルムの自然収縮を誘発し好ましく
ない。また、含有量が1wof%未満のフィルムでは、
十分なTgの低下が得られず好ましくない。For films with such content exceeding 25 mof%, Tg
This is not preferable because it causes a significant decrease in the film temperature and induces natural shrinkage of the film. In addition, in a film with a content of less than 1 wof%,
This is not preferable because a sufficient reduction in Tg cannot be obtained.
本発明で用いられる共重合ポリエステルにおいては、ジ
カルボン酸成分の好ましくは70モル%以上、より好ま
しくは75モル%以上がテレフタル酸単位であり、ジオ
ール成分の好ましくは70モル%以上、より好ましくは
75モル%以上がエチレングリコール単位である。テレ
フタル酸及び/又はエチレングリコール単位が70モル
%未満の共重合ポリエステルは、フィルムにした際のフ
ィルムの強度、耐溶剤性が劣るので好ましくない。In the copolymerized polyester used in the present invention, preferably 70 mol% or more of the dicarboxylic acid component, more preferably 75 mol% or more, is terephthalic acid units, and preferably 70 mol% or more, more preferably 75 mol% or more of the diol component. More than mol% is ethylene glycol units. A copolyester containing less than 70 mol % of terephthalic acid and/or ethylene glycol units is not preferred because the strength and solvent resistance of the film are poor when formed into a film.
また、上記ポリエステルは、該ポリエステル以外に30
−t%以下であれば他のポリマーを添加、混合したもの
でもよい。In addition, the above polyester may contain 30%
-t% or less, other polymers may be added or mixed.
さらに、フィルムの易滑性を向上させるために、有機滑
剤、無機の滑剤等の微粒子を含有させるのも好ましい。Furthermore, in order to improve the slipperiness of the film, it is also preferable to contain fine particles of an organic lubricant, an inorganic lubricant, or the like.
また、必要に応じて安定剤、着色剤、酸化防止剤、消泡
剤、静電防止剤等の添加剤を含有するものであってもよ
い。滑り性を付与する微粒子としては、カオリン、クレ
ー、炭酸カルシウム、酸化ケイ素、テレフタル酸カルシ
ウム、酸化アルミニウム、酸化チタン、リン酸カルシウ
ム、フッ化リチウム、カーボンブラック等の公知の不活
性外部粒子、ポリエステル樹脂の溶融製膜に際して不溶
な高融点有機化合物、架橋ポリマー及びポリエステル合
成時に使用する金属化合物触媒、例えばアルカリ金属化
合物、アルカリ土類金属化合物などによってポリエステ
ル製造時に、ポリマー内部に形成される内部粒子を挙げ
ることができる。フィルム中に含まれる微粒子の含有量
は、通常、O,OO5〜0.9重量%、該微粒子の平均
粒径は、通常、0.001〜3.5μmの範囲である。Moreover, additives such as stabilizers, colorants, antioxidants, antifoaming agents, and antistatic agents may be contained as necessary. Fine particles that impart slipperiness include known inert external particles such as kaolin, clay, calcium carbonate, silicon oxide, calcium terephthalate, aluminum oxide, titanium oxide, calcium phosphate, lithium fluoride, and carbon black, and melted polyester resin. Examples include internal particles formed inside the polymer during polyester production by insoluble high-melting point organic compounds during film formation, crosslinked polymers, and metal compound catalysts used during polyester synthesis, such as alkali metal compounds and alkaline earth metal compounds. can. The content of fine particles contained in the film is usually 5 to 0.9% by weight of O, OO, and the average particle size of the fine particles is usually in the range of 0.001 to 3.5 μm.
本発明においてフィルムに融解熱は好ましくは1〜8c
al!/g、更に好ましくは2〜6caIl/gである
。フィルムの融解熱が1caf/g未満のものでは押出
成膜前の乾燥工程で、通常のポリエチレンテレフタレー
トに用いられる乾燥方法が採用困難となり好ましくない
。また、融解熱が8caI!。In the present invention, the heat of fusion of the film is preferably 1 to 8 c.
Al! /g, more preferably 2 to 6 cal/g. If the heat of fusion of the film is less than 1 caf/g, it will be difficult to use the drying method normally used for polyethylene terephthalate in the drying step before extrusion film formation, which is not preferable. Also, the heat of fusion is 8caI! .
7gを越えるフィルムでは十分な収縮率が得られず好ま
しくない。If the weight exceeds 7 g, a sufficient shrinkage rate cannot be obtained, which is not preferable.
本発明のフィルムの極限粘度は、好ましくは0.50以
上、更に好ましくは0.60以上、特に好ましくは0.
65以上である。フィルムの極限粘度が0.50未満で
あると結晶性が高くなり、十分な収縮率が得られなくな
り好ましくない。The intrinsic viscosity of the film of the present invention is preferably 0.50 or more, more preferably 0.60 or more, particularly preferably 0.
It is 65 or more. If the intrinsic viscosity of the film is less than 0.50, crystallinity becomes high and sufficient shrinkage cannot be obtained, which is not preferable.
本発明のフィルムは、100℃エアーオーブン中で5分
間処理後の収縮率が、フィルムの横方向(主収縮方向)
において40%以上のものであり、かかる収縮率は、好
ましくは45%以上、更に好ましくは50%以上である
。フィルムの横方向の収縮率が40%未満のフィルムで
は、収縮量が不十分なため、ラベル用として使用するこ
とができない。The film of the present invention has a shrinkage rate in the lateral direction (main shrinkage direction) of the film after being treated in an air oven at 100°C for 5 minutes.
The shrinkage rate is preferably 45% or more, more preferably 50% or more. A film having a transverse shrinkage rate of less than 40% cannot be used for labels because the amount of shrinkage is insufficient.
本発明のフィルムは、100°Cエアーオープン中で5
分間処理後の収縮率が、フィルムの縦方向、すなわち主
収縮方向と直交する方向において20%以下のものであ
り、かかる収縮率は、好ましくは15%以下、更に好ま
しくは10%以下である。The film of the present invention is
The shrinkage rate after the minute treatment is 20% or less in the longitudinal direction of the film, that is, the direction perpendicular to the main shrinkage direction, and the shrinkage rate is preferably 15% or less, more preferably 10% or less.
縦方向の収縮率が20%を超えるフィルムでは、収縮時
に歪みや端部のカール等が発生するため、ラベルの外観
が不良となり、実用に供することができない。If the shrinkage rate in the longitudinal direction exceeds 20%, distortion or curling of the edges will occur during shrinkage, resulting in poor appearance of the label and cannot be put to practical use.
本発明のフィルムは、75°C温水中で5秒間処理後の
フィルム横方向の収縮率が通常、30%以上、好ましく
は35%以上、更に好ましくは40%以上のものである
。同条件におけるフィルム縦方向の収縮率は、好ましく
は10%以下、更に好ましくは5%以下である。The film of the present invention generally has a shrinkage rate in the transverse direction of the film after being treated in 75° C. hot water for 5 seconds, preferably 30% or more, preferably 35% or more, and more preferably 40% or more. The shrinkage rate of the film in the longitudinal direction under the same conditions is preferably 10% or less, more preferably 5% or less.
非耐熱性PETボトル用で用いられるシュリンクトンネ
ルは、収縮ゾーンの設定温度が80°C未満と低いため
、上記条件における主収縮方向の収縮率が30%未満の
フィルムでは十分に容器に密着することが出来ず好まし
くない。また、主収縮方向と直角方向の収縮率が10%
を超えるフィルムでは、収縮後、フィルムの図柄に歪み
が生じ、ラベル用収縮フィルムとして好ましくない。Shrink tunnels used for non-heat resistant PET bottles have a low set temperature in the shrink zone of less than 80°C, so a film with a shrinkage rate of less than 30% in the main shrinkage direction under the above conditions will not adhere well to the container. It is not possible and not desirable. In addition, the shrinkage rate in the direction perpendicular to the main shrinkage direction is 10%.
If the film exceeds this value, the design of the film will be distorted after shrinkage, making it undesirable as a shrink film for labels.
本発明のフィルムの主収縮方向の両端部を固定し、75
°C温水中で5秒間処理後の主収縮方向と直交する方向
の最大の収縮率(以下、ネ・ンクイン率とする)は通常
、20%以下であり、好ましくは18%以下、更に好ま
しくは15%以下である。Both ends of the film of the present invention in the main shrinkage direction are fixed, and
The maximum shrinkage rate in the direction perpendicular to the main shrinkage direction after treatment in °C warm water for 5 seconds (hereinafter referred to as "nequin ratio") is usually 20% or less, preferably 18% or less, more preferably It is 15% or less.
本発明において、ネックイン率は、主収縮方向が13c
m、該方向と直交する方向が10cmである長方形のサ
ンプルにおいて測定したものであり、この大きさは一般
的に使用されている収縮ラベルの折り径長と中長の、各
平均的な値である。ネ・ンクイン率は、シュリンクトン
ネル通過後のフィルムの斜め被り、フィルムの歪みとい
った収縮斑と密接に関連している。すなわち、ネックイ
ン率が20%を超えるフィルムは、収縮斑が頻発し、実
用上甚だ好ましくない。In the present invention, the neck-in rate is 13c in the main contraction direction.
m, measured on a rectangular sample with a direction perpendicular to this direction of 10 cm, and this size is the average value of the folded diameter length and medium length of commonly used shrink labels. be. The shrinkage rate is closely related to shrinkage spots such as diagonal overlapping of the film and distortion of the film after passing through the shrink tunnel. That is, a film with a neck-in rate exceeding 20% frequently suffers from shrinkage spots, which is extremely undesirable from a practical standpoint.
ネックイン率が大きいと収縮斑が発生しやすい原因は定
かではないが、本発明者らの考察は、以下の通りである
。The reason why shrinkage spots are more likely to occur when the neck-in rate is large is not clear, but the inventors' considerations are as follows.
ネックイン率が大きいフィルムは、主収縮方向を固定さ
れたときに、主収縮方向に作用すべき収縮応力が、該方
向と直角方向にかなりの割合で作用しているものと考え
られる。このようなフィルムでは実際にラベル用収縮フ
ィルムとして容器、特にボトルに装着後収縮させる際に
、主収縮方向に沿ってボトルの最大外形部にフィルムが
密着した直後、主収縮方向と直角方向に大きな収縮応力
が発生し、主収縮方向に収縮中のフィルム部位の収縮挙
動は極めて不安定なものになり、その結果、フィルムの
斜め被りゃ歪みといった収縮斑が発生するものと思われ
る。It is considered that in a film with a high neck-in ratio, when the main shrinkage direction is fixed, a considerable proportion of the shrinkage stress that should act in the main shrinkage direction acts in a direction perpendicular to the main shrinkage direction. When this type of film is actually used as a shrink film for labels and is shrunk after being attached to a container, especially a bottle, immediately after the film comes into close contact with the largest external part of the bottle along the main shrink direction, there is a large amount of shrinkage in the direction perpendicular to the main shrink direction. Shrinkage stress is generated, and the shrinkage behavior of the film portion that is shrinking in the main shrinkage direction becomes extremely unstable, and as a result, it is thought that shrinkage spots such as diagonal overlapping and distortion of the film occur.
本発明のフィルムは、上記収縮特性、特に100℃エア
ーオープン中で5分間処理後の収縮特性に加え、フィル
ムの縦方向の破断伸度が250%以上であることが必要
である。本発明でいう破断伸度とは、15mm巾、25
mm長のサンプルを50Qan/minの引張速度で引
張ったときの破断時伸度を指す。In addition to the above-mentioned shrinkage properties, particularly the shrinkage properties after being treated in an air open environment at 100° C. for 5 minutes, the film of the present invention is required to have a longitudinal elongation at break of 250% or more. The elongation at break as used in the present invention is 15 mm width, 25
It refers to the elongation at break when a mm-long sample is pulled at a tensile speed of 50 Qan/min.
破断伸度は、フィルムの縦方向の引裂は現像と密接な関
連があり、破断伸度が250%未満のフィルムでは、ラ
ベル用に加工する際に破断が頻発する。破断伸度は、好
ましくは300%以上、更に好ましくは350%以上、
特に好ましくは400%以上である。Regarding the elongation at break, longitudinal tearing of the film is closely related to development, and films with an elongation at break of less than 250% frequently break when processed for labels. The elongation at break is preferably 300% or more, more preferably 350% or more,
Particularly preferably, it is 400% or more.
本発明のフィルムの複屈折率は、通常、0.005以上
であり、好ましくは0.030〜0.150の範囲であ
る。複屈折率が0.005未満のフィルムでは、耐溶荊
性が劣り、ラベル用として印刷を施す際に問題となる。The birefringence of the film of the present invention is usually 0.005 or more, preferably in the range of 0.030 to 0.150. A film with a birefringence index of less than 0.005 has poor welding resistance, which poses a problem when printing for labels.
また、複屈折率が0.150を超えるフィルムは、収縮
時に歪みが生じやすくなる。Furthermore, a film with a birefringence index exceeding 0.150 tends to be distorted during shrinkage.
次に、本発明のフィルムの製造法を具体的に説明するが
、本発明の要旨を超えない限り、下記製造法に特に限定
されるものではない。Next, the manufacturing method of the film of the present invention will be specifically explained, but the method is not particularly limited to the following manufacturing method as long as it does not go beyond the gist of the present invention.
滑剤として無機粒子等を必要に応じて適量含有するポリ
エステルまたは共重合ポリエステルを、通常のホッパー
ドライヤー、パドルドライヤー真空乾燥機等を用いて乾
燥した後、200〜320°Cの温度で押出しを行う。A polyester or copolyester containing an appropriate amount of inorganic particles as a lubricant, if necessary, is dried using a conventional hopper dryer, paddle dryer vacuum dryer, etc., and then extruded at a temperature of 200 to 320°C.
押出しに際してはTダイ法、チューブラ法等、既存のど
の方法を採用しても構わない。For extrusion, any existing method such as the T-die method or the tubular method may be used.
押出し後、急冷して未延伸フィルムを得るが、Tダイ法
を用いた場合、急冷時にいわゆる静電印加密着法を採用
すれば、厚さ斑の均一なフィルムを得ることができ好ま
しい。After extrusion, the film is rapidly cooled to obtain an unstretched film. When using the T-die method, it is preferable to employ the so-called electrostatic application adhesion method during the rapid cooling, since a film with uniform thickness can be obtained.
得られた未延伸フィルムを加熱縦延伸ロールを用い、複
屈折率(ΔnI)が0.005〜0.050、好ましく
はO,OO5〜0.030の範囲となるように、縦方向
に1段又は2段以上で、1.1〜2.0倍延伸する。次
いで該縦1軸延伸フィルムを複屈折率(△n2)が0.
040以下、好ましくは0.030以下になるように、
縦方向に0.70〜0.98倍縦方向に弛緩する。縦弛
緩はロール間で行う方法が好ましく、特に、縦延伸後、
冷却することなく連続的に縦方向に弛緩する方法が好ま
しい。また、縦延伸後の複屈折率△n、および縦弛緩後
の複屈折率Δn2の比Δn+/Δn2は0.95以下に
することが好ましい。△n1/Δn2が0.95を超え
る場合は、フィルムの縦方向の収縮率が大きくなり過ぎ
好ましくない。The obtained unstretched film is stretched one step in the longitudinal direction using a heated longitudinal stretching roll so that the birefringence index (ΔnI) is in the range of 0.005 to 0.050, preferably in the range of O,OO5 to 0.030. Or, it is stretched 1.1 to 2.0 times in two or more stages. Next, the longitudinally uniaxially stretched film was adjusted to have a birefringence index (△n2) of 0.
040 or less, preferably 0.030 or less,
Relax in the machine direction by 0.70 to 0.98 times in the machine direction. It is preferable to perform longitudinal relaxation between rolls, especially after longitudinal stretching.
A method of continuous longitudinal relaxation without cooling is preferred. Further, the ratio Δn+/Δn2 of the birefringence index Δn after longitudinal stretching and the birefringence index Δn2 after longitudinal relaxation is preferably 0.95 or less. When Δn1/Δn2 exceeds 0.95, the shrinkage rate of the film in the longitudinal direction becomes too large, which is not preferable.
縦方向に延伸及び弛緩されたフィルムをテンターを用い
て3.0倍以上の延伸倍率で横延伸を行うが、横延伸前
に100〜140°Cに加熱して、更に縦方向の収縮率
を緩和することも好ましい。The film stretched and relaxed in the machine direction is stretched horizontally using a tenter at a stretching ratio of 3.0 times or more, but before stretching, the film is heated to 100 to 140°C to further reduce the shrinkage rate in the machine direction. Relaxation is also preferred.
横延伸後、フィルムを60〜100°Cで0.01〜6
0秒、特に好ましくは0.01〜30秒熱処理を施すこ
とにより、フィルムの収縮特性を向上させることができ
る。熱処理は通常、緊張固定下で実施されるが、同時に
20%以下の弛緩または巾出しを行うことも可能である
。熱処理法としては加熱ロールに接触させる方法やテン
ター内でクリップに把持して行う方法等の既知の方法を
用いることができる。また、熱処理後再延伸を行うこと
も可能である。After transverse stretching, the film is heated at 60-100°C to 0.01-6
The shrinkage characteristics of the film can be improved by performing heat treatment for 0 seconds, particularly preferably from 0.01 to 30 seconds. Heat treatment is usually carried out under tension fixation, but at the same time it is also possible to perform relaxation or widening of up to 20%. As the heat treatment method, known methods such as a method of contacting with a heating roll or a method of holding the material with a clip in a tenter can be used. Further, it is also possible to perform re-stretching after heat treatment.
前記延伸工程中、延伸前、又は延伸後にフィルムの片面
又は両面にコロナ放電処理を施し、フィルムの印刷層等
に対する接着性を向上させることも可能である。It is also possible to perform a corona discharge treatment on one or both sides of the film during, before, or after the stretching process to improve the adhesion of the film to the printed layer or the like.
また、上記延伸工程中、延伸前または延伸後にフィルム
の片面又は両面に塗布を行い、フィルムの接着性、帯電
防止性、易滑性、遮光性等を向上させることも可能であ
る。Furthermore, during the above-mentioned stretching process, it is also possible to coat one or both sides of the film before or after stretching to improve the film's adhesion, antistatic properties, slipperiness, light-shielding properties, etc.
さらに、本発明のフィルムの片面又は両面において、発
泡性のインキ層を印刷したり、内部に気泡を持つ熱可望
性樹脂のフィルム、又はシートを積層してクツション性
を持たせ、ガラス瓶包装後の破瓶効果等を向上させるこ
とも可能である。そのような熱可望性樹脂としてはポリ
塩化ビニル、ポリエチレン、ポリプロピレン、ポリアク
リル系、ポリスチレン、ポリエステル等、既知のいかな
る熱可塑性樹脂を用いても構わない。Furthermore, on one or both sides of the film of the present invention, a foaming ink layer is printed, or a thermoplastic resin film or sheet with bubbles inside is laminated to give it cushioning properties. It is also possible to improve the bottle-breaking effect, etc. As such thermoplastic resin, any known thermoplastic resin such as polyvinyl chloride, polyethylene, polypropylene, polyacrylic, polystyrene, polyester, etc. may be used.
上記のようにして得られたフィルムの厚さは特に限定さ
れないが、ラベル用収縮フィルムとして好ましく用いら
れる厚さは10〜300μmであり、特に好ましくは1
5〜200μmである。The thickness of the film obtained as described above is not particularly limited, but the thickness preferably used as a shrink film for labels is 10 to 300 μm, particularly preferably 1
It is 5 to 200 μm.
以下、実施例により本発明を更に具体的に説明するが、
本発明はその要旨を超えない限り、これらの実施例に限
定されるものではない。Hereinafter, the present invention will be explained in more detail with reference to Examples.
The present invention is not limited to these examples unless it exceeds the gist thereof.
なお、フィルムの評価方法は以下に示す通りである。In addition, the evaluation method of the film is as shown below.
(1)フィルムの極限粘度〔η〕
試料200■をフェノール/テトラクロロエタン=50
150の混合溶媒20−に加え、約110℃で1時間加
熱後、30°Cで測定した。(1) Intrinsic viscosity of the film [η] Sample 200μ is phenol/tetrachloroethane = 50
It was added to a mixed solvent of 150 and 20°C, heated at about 110°C for 1 hour, and then measured at 30°C.
(2)収縮率
下記熱処理条件(a)及びら)にて、収縮率の測定を行
った。(2) Shrinkage rate The shrinkage rate was measured under the following heat treatment conditions (a) and et al.
(a)100℃エアーオーブン
1cI1幅10C11長の短冊状としたフィルムを10
0±2℃の温度に調整されたギャードオーフン中に無荷
重の状態で5分間保持し、下記式に従い収縮率を求めた
。(a) 100℃ air oven 1cI1 width 10C11 length strip of film 10
The sample was held in a guarded oven with no load for 5 minutes at a temperature of 0±2° C., and the shrinkage rate was determined according to the following formula.
〔!:収縮後の長さ(am))
b) 75°C温水
フィルムを10cmX10cmの正方形とし、75±0
.5℃の温水中に無荷重の状態で5秒間保持して熱収縮
させた後、フィルムの縦および横方向について下記式に
従い求めた。[! : Length after shrinkage (am)) b) A 75°C hot water film is made into a 10cm x 10cm square, and the length is 75±0.
.. After heat-shrinking the film by holding it in 5° C. hot water for 5 seconds under no load, the longitudinal and transverse directions of the film were determined according to the following formula.
(3) ネックイン率
フィルムを横方向に長さ13C111以上、巾10cm
の長方形に切り出し、内寸13■長X10cm巾の金具
にフィルム横方向の両端を固定後、75±0.5°Cの
温水中で処理し、縦方向の最大の収縮率を求め、フィル
ムのネックイン率とした。(3) Neck-in rate film with a length of 13C111 or more in the horizontal direction and a width of 10cm
Cut out a rectangle, fix both ends of the film in the horizontal direction to metal fittings with internal dimensions of 13cm long x 10cm wide, and then process it in hot water at 75±0.5°C to find the maximum shrinkage rate in the vertical direction. It was taken as the neck-in rate.
(4)フィルムのガラス転移温度 Tgフィルムを窒素
雰囲気下、300°Cにて5分間加熱溶融し、象、冷し
て無定形状態にした後、セイコー電子工業銖製差動熱量
計5SC580DSC20型により昇温速度4°(:/
minにて’rgを測定した。Tgはベースラインが吸
熱側に偏岐し始めた温度T、と、新たなベースラインに
落ち着いた温度T2の算術平均値とした。(4) Glass transition temperature of the film The Tg film was heated and melted at 300°C for 5 minutes in a nitrogen atmosphere, cooled to an amorphous state, and then measured using a differential calorimeter 5SC580DSC20 model manufactured by Seiko Electronics Co., Ltd. Heating rate 4° (:/
'rg was measured at min. Tg was defined as the arithmetic mean value of the temperature T at which the baseline began to diverge to the endothermic side and the temperature T2 at which the baseline settled to the new baseline.
(5)複屈性率△n
カールツアイス社製偏光顕微鏡により、リターデーショ
ンを測定し、次式により複屈折率(△n)を求めた。(5) Birefringence Δn Retardation was measured using a polarizing microscope manufactured by Carl Zeiss, and the birefringence (Δn) was determined using the following formula.
△n = R/ d
(6)面配向度 △P
アタゴ社■製アツベ屈折計を用い、光源をナトリウムラ
ンプとして、フィルムの屈折率の測定を行った。Δn=R/d (6) Degree of Planar Orientation ΔP The refractive index of the film was measured using an Atsube refractometer manufactured by Atago Co., Ltd. and a sodium lamp as the light source.
フィルム面内の最大屈折率nr、それに直交する方向の
屈折率nβ、および厚さ方向の屈折率nαを求め、下記
式により面配向度へPを求めた。The maximum refractive index nr in the film plane, the refractive index nβ in the direction perpendicular thereto, and the refractive index nα in the thickness direction were determined, and the degree of plane orientation P was determined using the following formula.
△P=(nT−nβ)−nα
(7)フィルム縦方向の破断伸度
東洋ボールドウィン社製テンシロンを用い、20°C1
65%RHにて引張速度を500 mn/winとし、
15+m巾のサンプルを25mm間隔のチャックで固定
し、破断時の伸度を5本のサンプルについて測定し、そ
の平均値をフィルム縦方向の破断伸度とした。ΔP=(nT-nβ)-nα (7) Breaking elongation in the longitudinal direction of the film Using Tensilon manufactured by Toyo Baldwin Co., Ltd., 20°C1
The tensile speed was 500 mn/win at 65% RH,
Samples with a width of 15+m were fixed with chucks at intervals of 25 mm, and the elongation at break was measured for the five samples, and the average value was taken as the elongation at break in the longitudinal direction of the film.
(8)耐引裂性の評価
フィルムをラベル用フィルムとして、連続的に印刷、製
袋及び裁断の加工を行い、加工工程中において、破断が
なく、全く問題がないものを○、破断が頻発し実用上問
題があるものを×とした。(8) Evaluation of tear resistance The film is used as a label film and is continuously processed through printing, bag making, and cutting. During the processing process, there is no tearing and there is no problem at all. Items with practical problems were marked as ×.
(9)収縮特性の評価
フィルムを円筒形にして円筒状のボトルにかぶせた後、
シュリンクトンネルを通過させてボトルに装着させ、収
縮特性フィルムを評価した。ラベルの図柄の歪みがなく
密着性も優れ、美しい仕上りのものを◎、外観等が若干
劣るが実用上全く問題ないものを○、実用レベルに達し
ていないものを×とした。(9) Evaluation of shrinkage characteristics After making the film into a cylindrical shape and covering it over a cylindrical bottle,
The shrink properties of the film were evaluated by passing it through a shrink tunnel and attaching it to a bottle. Labels with no distortion of the design, excellent adhesion, and a beautiful finish were rated ◎, labels with slightly inferior appearance but no problem in practical use were rated ○, and labels that did not reach a practical level were rated ×.
実用例1
ジカルボン酸成分としてテレフタル酸単位80mof%
、イソフタル酸単位20mof%、ジオール成分として
エチレングリコール単位98mof%、ジエチレングリ
コール単位2mof%よりなり、平均粒径0.8μmの
球状シリカを500ppm含む共重合ポリエステル(〔
η)=0.70、Tg=66°C)を、パドルドライヤ
ーにより予備結晶化後、本乾燥を行い、260°Cで押
出機より押出し、急冷固化して未延伸フィルムを得た。Practical example 1 80 mof% terephthalic acid unit as dicarboxylic acid component
, a copolymerized polyester ([
η)=0.70, Tg=66°C) was pre-crystallized using a paddle dryer, then main drying was performed, extruded from an extruder at 260°C, and rapidly solidified to obtain an unstretched film.
得られたフィルムを80℃の延伸ロールで縦方向に1.
4倍延伸し、冷却することなく連続的に延伸ロールと冷
却ロールとの間で、縦方向に0.90倍縦縁緩した。次
いでフィルムをテンターに導いて、120°Cで熱処理
した後、85°Cで横方向に4.5倍延伸し、80°C
にて熱処理した後、冷却し平均厚さ40μmのフィルム
を得た。The obtained film was stretched 1.
The film was stretched 4 times, and the longitudinal edges were loosened by 0.90 times in the machine direction between a stretching roll and a cooling roll continuously without cooling. The film was then introduced into a tenter, heat treated at 120°C, stretched 4.5 times in the transverse direction at 85°C, and then stretched at 80°C.
After heat treatment, the film was cooled to obtain a film with an average thickness of 40 μm.
実施例2
実施例1において120°Cの熱処理を行わない他は実
施例1と同様にして平均厚さ40μmのフィルムを得た
。Example 2 A film with an average thickness of 40 μm was obtained in the same manner as in Example 1, except that the heat treatment at 120° C. was not performed.
比較例1
実施例1の未延伸フィルムを直接テンターに導いて、実
施例1と同様に横方向に延伸及び熱処理をし、平均厚さ
40μmのフィルムを得た。Comparative Example 1 The unstretched film of Example 1 was directly introduced into a tenter, and was laterally stretched and heat treated in the same manner as in Example 1 to obtain a film with an average thickness of 40 μm.
比較例2
実施例1の未延伸フィルムを80°Cの延伸ロール及び
冷却ロールを用い縦方向に1.4倍延伸した。Comparative Example 2 The unstretched film of Example 1 was stretched 1.4 times in the longitudinal direction using a stretching roll and a cooling roll at 80°C.
次いで該フィルムをテンターに導いて、実施例1と全く
同様にして120 ’Cで加熱したのち、横方向に延伸
及び熱処理をし、平均厚さ40μmのフィルムを得た。The film was then introduced into a tenter, heated at 120'C in exactly the same manner as in Example 1, and then stretched and heat-treated in the transverse direction to obtain a film with an average thickness of 40 μm.
以上、得られた結果をまとめて下記表1に示す。The results obtained above are summarized in Table 1 below.
〔発明の効果]
本発明のラベル用収縮フィルムは、優れた収縮特性およ
び強度を有しており、その工業的価値は高い。[Effects of the Invention] The shrink film for labels of the present invention has excellent shrink characteristics and strength, and has high industrial value.
Claims (1)
ルムの収縮率が横方向において40%以上であり、縦方
向において20%以下であり、かつ、フィルムの縦方向
の破断伸度が250%以上であることを特徴とするラベ
ル用ポリエステル系収縮フィルム。(1) The shrinkage rate of the film after being treated in an air open environment at 100°C for 5 minutes is 40% or more in the transverse direction and 20% or less in the longitudinal direction, and the elongation at break in the longitudinal direction of the film is 250%. A polyester shrink film for labels characterized by the above characteristics.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17219190A JPH0459333A (en) | 1990-06-29 | 1990-06-29 | Polyester shrink film for label |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17219190A JPH0459333A (en) | 1990-06-29 | 1990-06-29 | Polyester shrink film for label |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0459333A true JPH0459333A (en) | 1992-02-26 |
Family
ID=15937266
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17219190A Pending JPH0459333A (en) | 1990-06-29 | 1990-06-29 | Polyester shrink film for label |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0459333A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05318587A (en) * | 1992-05-21 | 1993-12-03 | Toyobo Co Ltd | Heat shrinkable polyester series film |
JPH071583A (en) * | 1993-06-22 | 1995-01-06 | Toyobo Co Ltd | Antistatic heat-shrinkable polyester film |
JPH11277625A (en) * | 1998-03-30 | 1999-10-12 | Toyobo Co Ltd | Heat shrinkable polyester film |
JP2002011790A (en) * | 2000-04-27 | 2002-01-15 | Toyobo Co Ltd | Heat-shrinkable thermoplastic resin-base film |
KR100731470B1 (en) * | 1999-10-04 | 2007-06-21 | 도요 보세키 가부시키가이샤 | Heat-shrinkable polyester films |
JP2008274160A (en) * | 2007-05-01 | 2008-11-13 | Toyobo Co Ltd | Heat-shrinkable polyester film, and method for producing the same |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6327535A (en) * | 1986-07-18 | 1988-02-05 | Diafoil Co Ltd | Shrinkable polyester film |
JPS63122519A (en) * | 1986-11-12 | 1988-05-26 | Diafoil Co Ltd | Polyester shrink film |
JPS63139725A (en) * | 1986-12-02 | 1988-06-11 | Diafoil Co Ltd | Polyester group shrinkable film |
JPS63202429A (en) * | 1987-02-17 | 1988-08-22 | Diafoil Co Ltd | Polyester shrink film excellent in heat-sealing property |
JPH0216032A (en) * | 1988-07-05 | 1990-01-19 | Diafoil Co Ltd | Polyester shrinkable film |
-
1990
- 1990-06-29 JP JP17219190A patent/JPH0459333A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6327535A (en) * | 1986-07-18 | 1988-02-05 | Diafoil Co Ltd | Shrinkable polyester film |
JPS63122519A (en) * | 1986-11-12 | 1988-05-26 | Diafoil Co Ltd | Polyester shrink film |
JPS63139725A (en) * | 1986-12-02 | 1988-06-11 | Diafoil Co Ltd | Polyester group shrinkable film |
JPS63202429A (en) * | 1987-02-17 | 1988-08-22 | Diafoil Co Ltd | Polyester shrink film excellent in heat-sealing property |
JPH0216032A (en) * | 1988-07-05 | 1990-01-19 | Diafoil Co Ltd | Polyester shrinkable film |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05318587A (en) * | 1992-05-21 | 1993-12-03 | Toyobo Co Ltd | Heat shrinkable polyester series film |
JPH071583A (en) * | 1993-06-22 | 1995-01-06 | Toyobo Co Ltd | Antistatic heat-shrinkable polyester film |
JPH11277625A (en) * | 1998-03-30 | 1999-10-12 | Toyobo Co Ltd | Heat shrinkable polyester film |
KR100731470B1 (en) * | 1999-10-04 | 2007-06-21 | 도요 보세키 가부시키가이샤 | Heat-shrinkable polyester films |
JP2002011790A (en) * | 2000-04-27 | 2002-01-15 | Toyobo Co Ltd | Heat-shrinkable thermoplastic resin-base film |
JP2008274160A (en) * | 2007-05-01 | 2008-11-13 | Toyobo Co Ltd | Heat-shrinkable polyester film, and method for producing the same |
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