JPH06114934A - Manufacture of thermally shrinkable polyester series film - Google Patents

Manufacture of thermally shrinkable polyester series film

Info

Publication number
JPH06114934A
JPH06114934A JP29635192A JP29635192A JPH06114934A JP H06114934 A JPH06114934 A JP H06114934A JP 29635192 A JP29635192 A JP 29635192A JP 29635192 A JP29635192 A JP 29635192A JP H06114934 A JPH06114934 A JP H06114934A
Authority
JP
Japan
Prior art keywords
glass transition
film
temperature
transition temperature
shrinkage
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
Application number
JP29635192A
Other languages
Japanese (ja)
Inventor
Tokuji Abe
徳治 阿部
Takeji Yanagisawa
武二 柳沢
Seiji Hashimoto
清治 橋本
Toshishige Arai
利重 荒井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP29635192A priority Critical patent/JPH06114934A/en
Publication of JPH06114934A publication Critical patent/JPH06114934A/en
Pending legal-status Critical Current

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  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To obtain a film having thermal shrinking characteristics of the same degree as that of a polyvinyl chloride series film having no shrinkage irregularity and excellent strength and shrinking characteristics by preheating a film made of polyethylene terephthalate series polymer and polyarylate resin, uniaxially orienting it, and thermally fixing it. CONSTITUTION:A polyester series resin composition having a glass transition temperature of 50-80 deg.C in which 20-60wt.% of polyarylate resin is mixed with polyethylene terephthalate series polymer is extrusion molded in a film state. Then, the film is preheated to a temperature range of the glass transition temperature to (glass transition temperature +20 deg.C). Thereafter, it is uniaxially oriented twice or more in a temperature range of (glass transition temperature +10 deg.C) to (crystallizing temperature -30 deg.C), further thermally fixed in a temperature range of further 45 deg.C or higher to less than the glass transition temperature, and subsequently cooled to the ambient temperature. Thus, a uniaxially oriented thermally shrinkable film having excellent tensile fracture elongation in a direction perpendicular to the elongating direction is obtained.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はコーラ、ジュース、ビー
ル、カップヌードルなどの飲食品、医薬品、雑貨、工業
材料、文房具、玩具、工具、その他種々の商品につい
て、内容物や販売元を表示し包装するためのラベルやキ
ャップシールとして、異物の混入防止、乾電池の放電防
止、商品の酸化や吸湿による劣化防止、商品の展示中の
汚損防止のためのセフティシールドとして、あるいは複
数個束ねるための包装材料などとして用いられる、熱収
縮性ポリエステル系フィルムの製造方法に関するもので
ある。
BACKGROUND OF THE INVENTION The present invention displays the contents and distributors of food and drink such as cola, juice, beer and cup noodles, pharmaceuticals, miscellaneous goods, industrial materials, stationery, toys, tools and various other products. As a label or cap seal for packaging, to prevent foreign matter from entering, to prevent dry batteries from discharging, to prevent deterioration of products due to oxidation or moisture absorption, as a safety shield to prevent contamination during product display, or as a bundle for bundling The present invention relates to a method for producing a heat-shrinkable polyester film used as a material or the like.

【0002】[0002]

【従来の技術】最近、熱帯雨林の減少、物の燃焼により
発生する二酸化炭素ガスによる地球の温暖化、NOX
どによる酸性雨と森林破壊、フロンによるオゾン層破壊
と紫外線の増加に伴う皮膚がんの発生などの公害問題か
ら派生して「地球にやさしい」物の使用が求められるよ
うになってきた。このため、印刷性がよく、きれいな包
装ができることから、これまで専らポリ塩化ビニル系フ
ィルムが使用されてきた熱収縮性ラベルにおいても、塩
素化合物を含まない材料に切り替えて欲しいとの要望が
でてきて、透明性のよいポリエチレンテレフタレート
(以下PETとする)フィルムなどのポリエステル系フ
ィルムが取り上げられ開発が進められてきた。
2. Description of the Related Art Recently, there has been a decrease in tropical rain forests, global warming due to carbon dioxide gas generated by burning materials, acid rain and forest destruction due to NO x, etc. As a result of pollution problems such as the occurrence of cancer, the use of "earth-friendly" products has been required. For this reason, good printability and clean packaging are possible.Therefore, even in heat-shrinkable labels where polyvinyl chloride films have been used exclusively so far, there is a demand to switch to materials that do not contain chlorine compounds. As a result, polyester films such as polyethylene terephthalate (hereinafter referred to as PET) film having good transparency have been picked up and developed.

【0003】ポリエステル系フィルムは、これまで高い
物理的強度と非常に高い寸法安定性が求められていたの
で、特公昭30−5639号公報に見られるように、延伸した
フィルムを延伸温度より高い温度で熱処理していた。と
ころが上述したラベル等の包装材料では熱収縮性、とり
わけ本発明で対象とする瓶や缶などの容器に付けるラベ
ルにおいては一方向にだけ熱収縮する性質、すなわち一
軸方向熱収縮性が求められている。しかも、ラベル用途
はこれまで塩化ビニル系樹脂が主流であったことから塩
化ビニル系樹脂と同程度の熱収縮特性が要求され、例え
ば、特開昭51-88550号公報などに見られるような種々の
検討が進められてきた。しかし、特開平3-135534号公報
に見られるように、一種類のポリエステル系ポリマーだ
けでは塩化ビニル系フィルムのような熱収縮性を得るこ
とが困難で、ガラス転移温度の異なる2種類以上のポリ
マーをブレンドすることが必要とされてきた。
Since polyester films have been required to have high physical strength and very high dimensional stability, as shown in Japanese Examined Patent Publication No. 3039/5639, a stretched film is heated at a temperature higher than the stretching temperature. Had been heat treated in. However, in the packaging material such as the label described above, the heat shrinkability, especially in the label to be attached to the container such as a bottle or can targeted by the present invention, the property of heat shrinking only in one direction, that is, the uniaxial heat shrinkability is required. There is. Moreover, since vinyl chloride resins have been the mainstream for label applications, heat shrinkage characteristics similar to those of vinyl chloride resins are required. For example, various types as disclosed in JP-A-51-88550 are disclosed. Has been examined. However, as seen in Japanese Patent Laid-Open No. 3-135534, it is difficult to obtain heat shrinkability like a vinyl chloride film by using only one type of polyester polymer, and two or more types of polymers having different glass transition temperatures are used. Has been required to be blended.

【0004】一方、ポリ塩化ビニルの一軸方向熱収縮性
フィルムの製造方法では一般に横方向に延伸するテンタ
ー法が採用されていて、その一般的な条件はフィルムを
まずガラス転移温度Tg +(20〜30)℃の範囲で予熱し
た後、その前後の温度で幅方向に所望の倍率で延伸し、
ついで縦方向の歪みや保存時の収縮むらを緩和すると共
に熱収縮曲線の勾配を緩やかにすることを期待して、フ
ィルムのガラス転移温度Tg +10℃以上の温度で熱固定
するものである。この条件をそのままポリエステル系熱
収縮性フィルムの製造に適用すると、得られる熱収縮性
フィルムは延伸方向に対して直角方向の破断伸びが著し
く小さい5%以下の値になること、すなわち降伏点に達
するかどうかの状態で破断することが知られている。と
くに、筒状のラベルやキャップシールなどの製造では、
印刷、張り合せ、裁断などの種々の工程で単なる引張り
張力のほかに衝撃的な張力もかかるので、フィルムの抗
張力が弱く引っ張り伸びの小さいフィルムは、それらの
工程で破断して、その度に製造がストップするという不
都合を生じる。このため、抗張力が高く破断伸びが 100
%以上あって製造中に破断して工程が停止することのな
いフィルムの開発が望まれていた。
On the other hand, in the method for producing a uniaxial heat-shrinkable film of polyvinyl chloride, a tenter method of stretching in the transverse direction is generally adopted, and the general condition is that the film first has a glass transition temperature T g + (20 ~ 30) after preheating in the range of ° C., at the temperature before and after that, stretched in the width direction at the desired ratio,
Next, the film is heat-set at a temperature of glass transition temperature T g + 10 ° C. or higher in the hope that the strain in the longitudinal direction and the shrinkage unevenness during storage will be relaxed and the gradient of the heat shrinkage curve will be gentle. If these conditions are directly applied to the production of the polyester heat-shrinkable film, the heat-shrinkable film obtained has a value of 5% or less in which the elongation at break in the direction perpendicular to the stretching direction is extremely small, that is, the yield point is reached. It is known to break depending on whether or not. Especially in the manufacture of tubular labels and cap seals,
In various processes such as printing, laminating and cutting, impact tension is applied in addition to mere tensile tension.Therefore, films with low tensile strength and low tensile strength are ruptured in those processes and manufactured each time. It causes the inconvenience of stopping. Therefore, the tensile strength is high and the elongation at break is 100
It has been desired to develop a film that does not break during the production due to the above-mentioned percentage, and the process does not stop.

【0005】[0005]

【発明が解決しようとする課題】したがって、本発明の
目的は、透明性、耐熱性、機械的強度、耐薬品性に優
れ、しかも廃棄物処理に際して燃焼時の有毒ガスの発生
や燃焼炉を傷めるなどの問題の少ないポリエステル系フ
ィルムにおいて、従来市場で最も多用されてきたポリ塩
化ビニル系フィルムと同程度の熱収縮特性を有し、加熱
収縮時の収縮むらやあばた状のしわの発生が極めて少な
く、延伸方向と直角の方向での引張り破断伸びが 100%
以上、 100℃における延伸方向の収縮率が50%以上、延
伸方向と直角の方向での収縮率が10%以下である、一軸
方向熱収縮性フィルムを提供することにある。
Therefore, the object of the present invention is to have excellent transparency, heat resistance, mechanical strength and chemical resistance, and also to generate toxic gas during combustion and damage the combustion furnace during waste treatment. Polyester film, which has few problems such as the above, has the same heat shrinkage characteristics as the polyvinyl chloride film that has been used most in the market so far, and the occurrence of shrinkage unevenness and pucker wrinkles during heat shrinkage is extremely small. , 100% tensile elongation at break in the direction perpendicular to the stretching direction
As described above, it is an object of the present invention to provide a uniaxial heat-shrinkable film having a shrinkage in the stretching direction at 100 ° C. of 50% or more and a shrinkage in the direction perpendicular to the stretching direction of 10% or less.

【0006】[0006]

【課題を解決するための手段】本出願人は先にPET系
ポリマーに20〜60重量%のポリアリレートを配合してな
るガラス転移温度50〜80℃のポリエステル系組成物を押
出成形した後、横方向に一軸延伸して熱収縮性を付与し
たポリエステル系フィルムでは、塩化ビニル系フィルム
と同様の熱収縮性を有し、かつ加熱収縮時の収縮むらや
あばた状のしわの発生が極めて少ないものとなることを
見出した。本発明者らはこの組成物を用いて、さらに 1
00℃における延伸方向の収縮率を50%以上、延伸方向と
直角の方向での収縮率を10%以下および同方向での引張
り破断伸びを 100%以上にするための延伸条件について
検討を進めた。一軸方向延伸フィルムにおいて延伸方向
の引っ張り強度は大きいが直角方向の強度が小さくなる
のは、フィブリル化現象が起きるためと一般に考えられ
ている。この現象を防止するには特開昭62-91555号公報
に見られるような二軸延伸で対応する方法もあるが、こ
の方法には縦延伸の設備を必要とするだけでなく工程が
増える分だけ制御が複雑になる欠点がある。
The present applicant has previously extruded a polyester composition having a glass transition temperature of 50 to 80 ° C., which is obtained by blending a PET polymer with 20 to 60% by weight of polyarylate, and then, A polyester film that is uniaxially stretched in the transverse direction to impart heat shrinkage, has the same heat shrinkability as a vinyl chloride film, and has very little shrinkage unevenness or wrinkle-like wrinkles during heat shrinkage. I found that. We have used this composition to
We examined the stretching conditions to achieve a shrinkage of 50% or more in the drawing direction at 00 ° C, a shrinkage of 10% or less in the direction perpendicular to the drawing direction, and a tensile elongation at break of 100% or more in the same direction. . In the uniaxially stretched film, it is generally considered that the tensile strength in the stretching direction is large but the strength in the orthogonal direction is small because the fibrillation phenomenon occurs. To prevent this phenomenon, there is a method of dealing with biaxial stretching as shown in JP-A-62-91555, but this method requires equipment for longitudinal stretching and increases the number of steps. The only drawback is that the control becomes complicated.

【0007】本発明者らは一軸延伸法における延伸方向
と直角の方向での引張り破断伸びの小さくなる原因が、
ポリエステル系ポリマーの配向性、結晶性の大きさにあ
るものと考え、その改善には横方向の延伸での結晶化速
度と延伸速度、それに加えて延伸後の結晶化度をある特
定の範囲内に制御し、凍結するための冷却を行えばよい
ことに着目して、さらに検討を進めた。その結果、ポリ
エチレンテレフタレート系ポリマーに20〜60重量%のポ
リアリレート樹脂を配合してなるガラス転移温度が50〜
85℃のポリエステル系樹脂組成物をフィルム状に押出成
形した後、このフィルムをガラス転移温度以上、ガラス
転移温度+20℃までの温度範囲で予熱し、ついでガラス
転移温度+10℃以上、結晶化温度−30℃までの温度範囲
で一軸方向に2倍以上延伸し、さらに45℃以上、ガラス
転移温度未満の温度範囲で熱固定し、引き続き室温にま
で冷却すると、延伸方向と直角の方向での引張り破断伸
びが 100%以上、 100℃における熱収縮率が延伸方向で
50%以上、その直角方向で10%以下の、一軸方向性熱収
縮性フィルムとして非常に優れた特性を有するものにな
ることを見出し、本発明を完成した。
The inventors of the present invention are responsible for the decrease in tensile elongation at break in the direction perpendicular to the stretching direction in the uniaxial stretching method.
It is considered that the orientation and crystallinity of the polyester-based polymer lie in the degree of improvement.To improve it, the crystallization rate in the transverse stretching and the stretching rate, as well as the crystallinity after stretching within a certain range Further studies were conducted, focusing on the fact that it is sufficient to control the temperature and perform cooling for freezing. As a result, the glass transition temperature of polyethylene terephthalate-based polymer blended with 20 to 60% by weight of polyarylate resin is 50 to 50%.
After extrusion-molding a polyester resin composition at 85 ° C into a film, the film is preheated in a temperature range of glass transition temperature or higher and glass transition temperature + 20 ° C, then glass transition temperature + 10 ° C or higher, crystallization temperature- Tensile rupture in the direction perpendicular to the stretching direction when stretched in the uniaxial direction at least 2 times in the temperature range up to 30 ° C, further heat set in the temperature range above 45 ° C and below the glass transition temperature, and then cooled to room temperature. Elongation is 100% or more, thermal shrinkage at 100 ℃ in the stretching direction
The present invention has been completed by finding that the uniaxial heat-shrinkable film of 50% or more and 10% or less in the perpendicular direction has very excellent properties.

【0008】以下、本発明を詳細に説明する。一般にポ
リエステル系樹脂は、その成分組成によってガラス転移
点やブレンド対象レジンとの相溶性が大きく変化する。
ポリマーブレンドの比率によって見掛け上均一に相溶し
たり、相溶性が低下してマトリックス(海)部とその中
に分散する島状部との2相の形態が現われたりする。一
般のポリマーで均一に相溶した場合、単一ポリマーのよ
うにガラス転移温度前後での弾性率が急激に変化する。
しかし、微細に相分離したような2相(以上)が存在す
る状態のものでは、ガラス転移温度前後での弾性率は多
段的に変化するか、なだらかに温度変化する。本発明の
熱収縮性ポリエステル系フィルムの製造に用いられるポ
リエステル系組成物はPET系ポリマーとポリアリレー
トとからなるものが用いられる。
The present invention will be described in detail below. Generally, the polyester resin greatly changes in glass transition point and compatibility with a resin to be blended depending on its component composition.
Depending on the ratio of the polymer blend, they are apparently homogeneously compatible, or the compatibility is lowered, and a two-phase morphology of a matrix (sea) part and island-shaped parts dispersed therein appears. When a general polymer is uniformly compatible, the elastic modulus around the glass transition temperature changes rapidly like a single polymer.
However, in the state where there are two phases (or more) that are finely phase-separated, the elastic modulus around the glass transition temperature changes in multiple stages or changes gently. The polyester composition used for producing the heat-shrinkable polyester film of the present invention is composed of a PET polymer and polyarylate.

【0009】このPET系ポリマーはガラス転移温度が
40〜85℃のものがよく、これが40℃より低くなると、フ
ィルムの収縮開始温度が低くなり過ぎてフィルムの保管
中に部分的な収縮が起こるようになり、また85℃よりも
高くなると、フィルムの延伸温度が高くなるだけでなく
収縮開始温度も高くなり過ぎて加工上好ましくない。P
ET系ポリマーの組成はジカルボン酸成分とジオール成
分とからなり、ジカルボン酸の成分としてはテレフター
ル酸が70モル%以上、とくには85モル%以上のものが好
ましく、ガラス転移温度を高めたいときはこれにナフタ
レンジカルボン酸の10〜30モル%以下を組み合わせ、逆
にガラス転移温度を低めたいときはイソフタール酸、オ
ルトフタール酸、コハク酸、グルタル酸、アジピン酸、
セバシン酸、アゼライン酸、スペリン酸、シュウ酸、マ
ロン酸等の公知のジカルボン酸の中より相溶性などを考
慮しながら1種単独または2種以上を組み合わせて選択
使用すればよい。
This PET-based polymer has a glass transition temperature
40 ~ 85 ℃ is good, and if it is lower than 40 ℃, the shrinkage initiation temperature of the film becomes too low and partial shrinkage occurs during storage of the film, and if it is higher than 85 ℃, the film shrinks. Not only the stretching temperature becomes high but also the shrinkage starting temperature becomes too high, which is not preferable in processing. P
The composition of the ET polymer is composed of a dicarboxylic acid component and a diol component, and as the dicarboxylic acid component, terephthalic acid is preferably 70 mol% or more, particularly 85 mol% or more. In combination with 10 to 30 mol% or less of naphthalene dicarboxylic acid, and conversely to lower the glass transition temperature, isophthalic acid, orthophthalic acid, succinic acid, glutaric acid, adipic acid,
One of the known dicarboxylic acids such as sebacic acid, azelaic acid, speric acid, oxalic acid, and malonic acid may be used alone or in combination with two or more in consideration of compatibility.

【0010】ジオール成分としてはエチレングリコール
が70モル%以上、とくには90モル%以上のものが好まし
く、ガラス転移温度やブレンド対象レジンに対する相溶
性を考慮しながら、プロピレングリコール、ペンタンジ
オール、ヘキサンジオール、ネオペンチルグリコール、
ジエチレングリコール、トリエチレングリコール、ポリ
エチレングリコール、1,4−ブタンジオール、1,4
−シクロヘキサンジメタノール等の公知のジオール成分
の1種単独または2種以上の組み合わせで選択使用すれ
ばよい。上記2成分を組み合せて縮合反応することによ
り、前記PET系ポリマーとすることができる。
As the diol component, ethylene glycol of 70 mol% or more, particularly 90 mol% or more is preferable, and propylene glycol, pentanediol, hexanediol, propylene glycol, etc. are taken into consideration while taking into consideration the glass transition temperature and the compatibility with the resin to be blended. Neopentyl glycol,
Diethylene glycol, triethylene glycol, polyethylene glycol, 1,4-butanediol, 1,4
-A known diol component such as cyclohexanedimethanol may be used alone or in combination of two or more. The PET-based polymer can be obtained by combining the above two components and conducting a condensation reaction.

【0011】前記ポリエステル系組成物の他方の成分で
あるポリアリレートは、分子内に芳香族環を有するポリ
エステルで、これらの内ではテレフタル酸またはイソフ
タル酸とビスフェノールAとの重縮合体が好ましいが、
他のジフェノールと塩基酸との重縮合体でもPETとの
相溶性がほどほどにあって、しかもガラス転移温度が15
0〜 200℃の範囲のものであれば採用することができ
る。ここでガラス転移温度が 150℃よりも低いものは、
入手が困難なばかりでなくPET系ポリマーとのブレン
ドにより収縮温度範囲を広げる効果が小さくなる。また
ガラス転移温度が 200℃より高くなると、フィルム系全
体のガラス転移温度も高くなって延伸が困難になるばか
りでなく、収縮開始温度も高くなるので従来のシュリン
ク炉での加工に適さなくなる。
The other component of the polyester composition, polyarylate, is a polyester having an aromatic ring in the molecule, and among these, a polycondensate of terephthalic acid or isophthalic acid and bisphenol A is preferable,
Even polycondensates of other diphenols and basic acids have moderate compatibility with PET and have a glass transition temperature of 15
Any material in the range of 0 to 200 ° C can be used. Here, if the glass transition temperature is lower than 150 ° C,
Not only is it difficult to obtain, but blending with a PET-based polymer reduces the effect of expanding the shrinkage temperature range. On the other hand, if the glass transition temperature is higher than 200 ° C, not only the glass transition temperature of the entire film system becomes high and it becomes difficult to stretch, but also the shrinkage initiation temperature becomes high, which makes it unsuitable for processing in a conventional shrink furnace.

【0012】PET系ポリマーにポリアリレート樹脂を
ブレンドすると、そのブレンド比率に応じてガラス転移
温度が高くなると共に収縮開始温度も高くなる。このブ
レンド比率が20重量%未満では、熱収縮温度曲線の勾配
がPET系ポリマー単独の場合と同様に急勾配になる。
またこれが60重量%を超えると、ブレンド体のガラス転
移温度が上昇し、延伸温度が高くなり過ぎて80〜 110℃
での延伸が困難になるばかりでなく熱収縮開始温度も高
くなり過ぎる。熱収縮する温度が高くなることは、延伸
したフィルムを保管しているうちに自然収縮していびつ
になる心配はなくなるが、一般のシュリンクトンネル炉
での収縮が困難になる。これらの点を勘案してポリアリ
レート系樹脂のブレンド比率は20〜60重量%、好ましく
は20〜40重量%が適当である。このようにして得られる
ポリエステル系組成物は、均一なポリマー体、ブロック
ポリマー、ポリマーブレンド体など、その形態に拘わら
ず、ガラス転移温度が50〜85℃、好ましくは60〜85℃の
範囲にあることが必要で、これが50℃以下のものでは延
伸したフィルムが保管中に自然収縮を起こし、いびつに
なったりして商品に被せることができなくなる。またガ
ラス転移温度が85℃以上のものから得られた熱収縮性フ
ィルムでは、従来のシュリンク炉で高い生産性で収縮さ
せることが困難になる。なお、このポリエステル系組成
物には、上記ポリマー成分のほかに、必要に応じて安定
剤、滑剤、着色剤、酸化防止剤、静電気防止剤、フィル
ム同士の滑性を改良するための有機または無機の滑剤な
どを添加してもよい。
When a PET polymer is blended with a polyarylate resin, the glass transition temperature and the shrinkage onset temperature increase depending on the blending ratio. When the blend ratio is less than 20% by weight, the slope of the heat shrinkage temperature curve becomes steep as in the case of the PET polymer alone.
On the other hand, if it exceeds 60% by weight, the glass transition temperature of the blended product rises and the stretching temperature becomes too high, resulting in 80 to 110 ° C.
Not only becomes difficult to stretch but also the heat shrinkage initiation temperature becomes too high. When the temperature for heat shrinkage becomes high, there is no fear that the stretched film will naturally shrink during storage, but shrinkage in a general shrink tunnel furnace becomes difficult. Considering these points, the blending ratio of the polyarylate resin is 20 to 60% by weight, preferably 20 to 40% by weight. The polyester composition thus obtained has a glass transition temperature of 50 to 85 ° C., preferably 60 to 85 ° C., regardless of its form, such as a homogeneous polymer, block polymer, and polymer blend. If the temperature is less than 50 ° C, the stretched film will spontaneously shrink during storage and become distorted and cannot be put on the product. In addition, it is difficult to shrink a heat-shrinkable film having a glass transition temperature of 85 ° C or higher with a conventional shrink furnace with high productivity. In addition to the above-mentioned polymer components, the polyester-based composition contains, if necessary, a stabilizer, a lubricant, a colorant, an antioxidant, an antistatic agent, an organic or inorganic material for improving the lubricity between films. Lubricants and the like may be added.

【0013】本発明の方法による熱収縮性ポリエステル
系フィルムは、このポリエステル系組成物を、例えばT
ダイを用いてフィルム状に押出成形した後、このフィル
ムをガラス転移温度以上、ガラス転移温度+20℃までの
温度範囲で予熱し、ついでガラス転移温度+10℃以上、
結晶化温度−30℃までの温度範囲で縦横いずれかの一軸
方向に2倍以上、好ましくは 2.5倍以上延伸し、さらに
45℃以上、ガラス転移温度未満の温度範囲、好ましくは
50℃以上、ガラス転移温度−5℃の温度範囲で、好まし
くは 0.1〜 0.4分、とくに好ましくは 0.1〜 0.3分かけ
て熱固定し、引き続き室温にまで冷却することによって
得られる。
The heat-shrinkable polyester film produced by the method of the present invention is obtained by adding the polyester composition to, for example, T
After extrusion molding into a film using a die, this film is preheated in the temperature range of glass transition temperature or higher and glass transition temperature + 20 ° C, and then glass transition temperature + 10 ° C or higher,
Stretched in the temperature range up to -30 ° C in the uniaxial direction in either the longitudinal or transverse directions by a factor of 2 or more, preferably 2.5 or more.
A temperature range of 45 ° C or higher and lower than the glass transition temperature, preferably
It can be obtained by heat-setting in a temperature range of 50 ° C. or higher and a glass transition temperature of −5 ° C. for 0.1 to 0.4 minutes, particularly preferably 0.1 to 0.3 minutes, and then cooling to room temperature.

【0014】上記において、予熱がガラス転移温度未満
の温度で行われるときは、つぎの延伸工程で2倍以上に
延伸することが困難になり、ガラス転移温度+20℃を超
える温度で行われるときは、得られる熱収縮性ポリエス
テル系フィルムの厚さの均一性が損なわれ、 100℃にお
ける延伸方向の収縮率が50%未満となる。延伸がガラス
転移温度+10℃未満の温度で行われるときは、実装テス
トでの不良品の発生が多くなり、結晶化温度−30℃を超
える温度で行われるときは、得られるフィルムがすりガ
ラスのように曇ったり局部的に歪んだりするほか、延伸
方向と直角の方向での引っ張り切断伸びが低下する。ま
た延伸倍率が2倍に達しないときは、得られるフィルム
の 100℃における延伸方向の収縮率が50%未満となる。
熱固定が45℃未満の温度で行われるときは、延伸方向と
直角の方向での引っ張り切断伸びを 100%以上にするこ
とができるものの、 100℃における同方向での収縮率が
10%を超えるものとなり、ガラス転移温度を超える温度
で行われるときは、延伸方向と直角の方向での引っ張り
切断伸びが低下する。また熱固定時間が0.1分未満では
延伸方向と直角の方向での収縮率が高くなり、 0.4分を
超えると同方向での引っ張り切断伸びが低下する。
In the above, when the preheating is carried out at a temperature lower than the glass transition temperature, it becomes difficult to draw it at least twice in the next drawing step, and when it is carried out at a temperature higher than the glass transition temperature + 20 ° C. The thickness uniformity of the resulting heat-shrinkable polyester film is impaired, and the shrinkage ratio in the stretching direction at 100 ° C is less than 50%. When the stretching is carried out at a temperature lower than the glass transition temperature + 10 ° C, the number of defective products in the mounting test increases, and when the stretching is carried out at a temperature higher than -30 ° C, the obtained film looks like ground glass. In addition to being clouded and locally distorted, the tensile cutting elongation in the direction perpendicular to the stretching direction is reduced. When the draw ratio does not reach 2 times, the shrinkage ratio of the obtained film at 100 ° C in the drawing direction is less than 50%.
When heat setting is performed at a temperature lower than 45 ° C, the tensile cutting elongation in the direction perpendicular to the stretching direction can be 100% or more, but the shrinkage ratio in the same direction at 100 ° C is
When the temperature exceeds 10% and the temperature exceeds the glass transition temperature, the tensile cutting elongation in the direction perpendicular to the stretching direction decreases. Further, if the heat setting time is less than 0.1 minutes, the shrinkage ratio in the direction perpendicular to the stretching direction becomes high, and if it exceeds 0.4 minutes, the tensile cutting elongation in the same direction decreases.

【0015】[0015]

【実施例】以下、本発明の具体的態様を実験例により説
明するが、本発明はこれらの記載に限定されるものでは
ない。 実験 No.1〜5、10、11および13(本発明)、 No.6〜
9、12、14および15(比較例)並びに No.16(参考
例):表1および2に示すように、下記のPET系ポリ
マーとガラス転移温度が約 180℃のビスフェノール型ポ
リアリレート樹脂(表中ARと示す)とを混合し、熱風式
棚段乾燥機を用いて 150℃で6時間乾燥し、表1および
2に示すガラス転移温度と結晶化温度のポリエステル系
組成物を得た。 ・PET-1 ‥PETのみからなるポリマー、ガラス転移温
度:80℃。 ・PET-2 ‥テレフタール酸の一部を10モル%のセバシン
酸で置換したPET系ポリマー、ガラス転移温度:43
℃。 ・PET-3 ‥テレフタール酸の一部を5モル%のセバシン
酸と5モル%のイソフタール酸で置換したPET系ポリ
マー、ガラス転移温度:50℃。 ・PET-4 ‥テレフタール酸の一部を10モル%のイソフタ
ール酸で置換したPET系ポリマー、ガラス転移温度:
73℃。
EXAMPLES Hereinafter, specific embodiments of the present invention will be described with reference to experimental examples, but the present invention is not limited to these descriptions. Experiment Nos. 1 to 5, 10, 11 and 13 (invention), No. 6 to
9, 12, 14 and 15 (comparative example) and No. 16 (reference example): As shown in Tables 1 and 2, the following PET-based polymer and a bisphenol type polyarylate resin having a glass transition temperature of about 180 ° C. (table Medium AR) and mixed with a hot-air tray dryer at 150 ° C. for 6 hours to obtain polyester compositions having glass transition temperatures and crystallization temperatures shown in Tables 1 and 2.・ PET-1 ・ ・ ・ Polymer consisting of PET only, glass transition temperature: 80 ℃.・ PET-2: PET polymer in which a part of terephthalic acid is replaced with 10 mol% of sebacic acid, glass transition temperature: 43
° C. -PET-3: PET polymer in which a part of terephthalic acid is replaced with 5 mol% of sebacic acid and 5 mol% of isophthalic acid, glass transition temperature: 50 ° C. -PET-4: PET polymer in which a part of terephthalic acid is replaced with 10 mol% of isophthalic acid, glass transition temperature:
73 ° C.

【0016】これより、 100〜 110℃の乾燥窒素ガスを
流したホッパー付きの、口径(D)=40φ、L(押出機
長さ)/D=25の押出機でナイロンタイプスクリューを
用いてペレットを作り、引き続いて同じ押出機に幅 400
mm、リップ間隙 0.5mmのT−ダイを取りつけて、厚さ 1
00μm のフィルムを成形した。ペレット、フィルム成形
時共に、押出機の温度条件はC1 = 190℃、C2 = 280
℃、C3 = 300℃、ダイ温度= 300℃で、ペレット、フ
ィルム共に押出し後、ガラス転移温度以下に急冷した。
このフィルムを長さ10mの横一軸延伸機を用いて表1お
よび2に示した条件で延伸した後、熱固定し、直ちに室
温まで急冷して熱収縮性フィルムを得た。なお、実験 N
o.16は市販のポリ塩化ビニル系熱収縮性フィルム 40G
(信越化学工業社製)を使用した場合を参考例として示
した。以上の各フィルムについて、下記の測定を行い、
その結果を表1および2に併記した。
From this, pellets were formed using a nylon type screw in an extruder with a hopper in which a dry nitrogen gas of 100 to 110 ° C. was made to flow and a diameter (D) = 40φ, L (extruder length) / D = 25. Build and subsequently 400 width on the same extruder
mm, lip gap 0.5mm, T-die attached, thickness 1
A film of 00 μm was formed. Extruder temperature conditions are C 1 = 190 ° C., C 2 = 280 for both pellet and film forming.
℃, C 3 = 300 ℃, at die temperature = 300 ° C., pellets after extrusion into a film both were quenched to below the glass transition temperature.
This film was stretched using a transverse uniaxial stretching machine with a length of 10 m under the conditions shown in Tables 1 and 2, then heat-set and immediately cooled to room temperature to obtain a heat-shrinkable film. Experiment N
o.16 is a commercially available polyvinyl chloride heat-shrinkable film 40G
The case of using (manufactured by Shin-Etsu Chemical Co., Ltd.) is shown as a reference example. For each of the above films, perform the following measurements,
The results are also shown in Tables 1 and 2.

【0017】・引張り強度の測定:延伸したフィルムよ
りダンベル1号で試験片を打ち抜き、23℃、50%の高温
高湿の部屋に一昼夜放置した後、200mm/分の速度で引張
り、縦(表中MDとする)横(表中TDとする)両方向
の降伏値と破断伸びを測定する。 ・ 100℃での収縮率の測定:延伸したフィルムより10cm
×10cmの大きさの正方形の試験片を切り出し、 100℃の
熱湯浴槽に30秒間浸した後、縦横(上記と同じ)両方向
の収縮率を測定する。 ・実装性:25℃の水を充填した1リットルのPET製瓶
に、各フィルムを背貼りして調製したチューブ状のラベ
ルを被せ、90〜95℃に維持したスチ−ム式シュリンクト
ンネル炉を通して加熱収縮させたときの瓶の肩部や胴部
での収縮状態を観察して下記の基準で評価した。 ◎:収縮むらのないきれいな外観 ○:収縮むらのない外観 △:僅かに収縮むらが認められる外観 ×:収縮むらが著しい外観
Measurement of tensile strength: A test piece was punched out from a stretched film with dumbbell No. 1, left in a room at 23 ° C. and 50% high temperature and high humidity for one day and night, and then stretched at a speed of 200 mm / min, and longitudinal (table The yield value and the elongation at break are measured in both directions, which is defined as medium MD) and lateral direction (designated as TD in the table).・ Measurement of shrinkage at 100 ℃: 10cm from stretched film
Cut out a square test piece with a size of × 10 cm, dip it in a 100 ° C hot water bath for 30 seconds, and measure the shrinkage in both the vertical and horizontal directions (the same as above). -Mountability: A PET bottle of 1 liter filled with water at 25 ° C is covered with a tube-shaped label prepared by back-adhering each film, and passed through a steam shrink tunnel furnace maintained at 90 to 95 ° C. The shrinkage state at the shoulder and body of the bottle when heat-shrinked was observed and evaluated according to the following criteria. ◎: Clean appearance without shrinkage unevenness ○: Appearance without shrinkage unevenness △: Appearance with slight shrinkage unevenness ×: Appearance with remarkable shrinkage unevenness

【0020】[0020]

【発明の効果】本発明の方法によって得られた熱収縮性
ポリエステル系フィルムは、降伏値がいずれの方向でも
4.0kg/cm2 以上、延伸方向と直角の方向での引っ張り破
断伸びが 100%以上、 100℃での収縮率が延伸方向で50
%以上、延伸方向と直角の方向で10%以下であるほか、
実装テストにおいても良好な包装適性を示す。
The heat-shrinkable polyester film obtained by the method of the present invention has a yield value in any direction.
4.0 kg / cm 2 or more, tensile breaking elongation in the direction perpendicular to the stretching direction is 100% or more, and shrinkage at 100 ° C is 50 in the stretching direction.
% Or more and 10% or less in the direction perpendicular to the stretching direction,
Good packaging suitability in mounting test.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 橋本 清治 茨城県鹿島郡神栖町大字東和田1番地 信 越化学工業株式会社塩ビ技術研究所内 (72)発明者 荒井 利重 茨城県鹿島郡神栖町大字東和田1番地 信 越化学工業株式会社高分子機能性材料研究 所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Seiji Hashimoto, Inventor, Tohada, Kamisu-cho, Kashima-gun, Ibaraki Prefecture, Towada, Shin-Etsu Chemical Co., Ltd. Towada No. 1 Shin-Etsu Chemical Co., Ltd., Polymer Functional Materials Research Center

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ポリエチレンテレフタレート系ポリマーに
20〜60重量%のポリアリレート樹脂を配合してなるガラ
ス転移温度が50〜85℃のポリエステル系樹脂組成物をフ
ィルム状に押出成形した後、このフィルムをガラス転移
温度以上、ガラス転移温度+20℃までの温度範囲で予熱
し、ついでガラス転移温度+10℃以上、結晶化温度−30
℃までの温度範囲で一軸方向に2倍以上延伸し、さらに
45℃以上、ガラス転移温度未満の温度範囲で熱固定し、
引き続き室温にまで冷却することを特徴とする熱収縮性
ポリエステル系フィルムの製造方法。
1. A polyethylene terephthalate-based polymer
After extruding a polyester resin composition having a glass transition temperature of 50 to 85 ° C, which is prepared by blending 20 to 60% by weight of a polyarylate resin, into a film, the film is heated to a glass transition temperature or higher, a glass transition temperature + 20 ° C. Temperature range up to, glass transition temperature + 10 ℃ or more, crystallization temperature -30
Stretched more than 2 times in uniaxial direction in the temperature range up to ℃,
Heat set in the temperature range of 45 ° C or higher and lower than the glass transition temperature,
A method for producing a heat-shrinkable polyester film, which comprises subsequently cooling to room temperature.
JP29635192A 1992-10-08 1992-10-08 Manufacture of thermally shrinkable polyester series film Pending JPH06114934A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29635192A JPH06114934A (en) 1992-10-08 1992-10-08 Manufacture of thermally shrinkable polyester series film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29635192A JPH06114934A (en) 1992-10-08 1992-10-08 Manufacture of thermally shrinkable polyester series film

Publications (1)

Publication Number Publication Date
JPH06114934A true JPH06114934A (en) 1994-04-26

Family

ID=17832433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29635192A Pending JPH06114934A (en) 1992-10-08 1992-10-08 Manufacture of thermally shrinkable polyester series film

Country Status (1)

Country Link
JP (1) JPH06114934A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987005919A1 (en) * 1986-04-01 1987-10-08 Toray Industries, Inc. Biaxially oriented polyester film
JPH09187863A (en) * 1996-01-11 1997-07-22 Mitsubishi Plastics Ind Ltd Heat-shrinkable polylactic acid-based film and its production
KR100688347B1 (en) * 2005-10-12 2007-03-02 도레이새한 주식회사 Heat shrinkable film and preparing method thereof
JP2008540177A (en) * 2005-05-10 2008-11-20 トレオファン・ジャーマニー・ゲーエムベーハー・ウント・コンパニー・カーゲー Method and apparatus for transverse stretching a raw web
US20100331513A1 (en) * 2007-12-11 2010-12-30 Kolon Industries, Inc. Thermo-shrinkable polyester film

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987005919A1 (en) * 1986-04-01 1987-10-08 Toray Industries, Inc. Biaxially oriented polyester film
JPH09187863A (en) * 1996-01-11 1997-07-22 Mitsubishi Plastics Ind Ltd Heat-shrinkable polylactic acid-based film and its production
JP2008540177A (en) * 2005-05-10 2008-11-20 トレオファン・ジャーマニー・ゲーエムベーハー・ウント・コンパニー・カーゲー Method and apparatus for transverse stretching a raw web
KR100688347B1 (en) * 2005-10-12 2007-03-02 도레이새한 주식회사 Heat shrinkable film and preparing method thereof
US20100331513A1 (en) * 2007-12-11 2010-12-30 Kolon Industries, Inc. Thermo-shrinkable polyester film
US8568841B2 (en) * 2007-12-11 2013-10-29 Kolon Industries, Inc. Thermo-shrinkable polyester film

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