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JPH0329763A - Fluorescent-lamp shrink packaging polyester film - Google Patents

Fluorescent-lamp shrink packaging polyester film

Info

Publication number
JPH0329763A
JPH0329763A JP15259389A JP15259389A JPH0329763A JP H0329763 A JPH0329763 A JP H0329763A JP 15259389 A JP15259389 A JP 15259389A JP 15259389 A JP15259389 A JP 15259389A JP H0329763 A JPH0329763 A JP H0329763A
Authority
JP
Japan
Prior art keywords
film
shrinkage
polyester
oriented
rate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP15259389A
Other languages
Japanese (ja)
Other versions
JP2692270B2 (en
Inventor
Satoyuki Kotani
小谷 智行
Yujiro Fukuda
裕二郎 福田
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.)
Diafoil Co Ltd
Original Assignee
Diafoil 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 Diafoil Co Ltd filed Critical Diafoil Co Ltd
Priority to JP15259389A priority Critical patent/JP2692270B2/en
Publication of JPH0329763A publication Critical patent/JPH0329763A/en
Application granted granted Critical
Publication of JP2692270B2 publication Critical patent/JP2692270B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Vessels And Coating Films For Discharge Lamps (AREA)
  • Packages (AREA)
  • Wrappers (AREA)

Abstract

PURPOSE:To reduce wrinkling and distortion of a film, etc., at the time of shrink packaging and to contrive to improve working properties of the film by giving certain specific physical properties to a biaxially oriented film. CONSTITUTION:After polyester or copolymer polyester containing the proper quantity of inorganic particles, etc., as lubricant has been dried by the use of hopper dryer, paddle dryer, vacuum dryer, etc., the extraction of the polyester is performed at the temperature of 200-320 deg.C. Non-oriented film obtained by quenching after the extraction is first oriented 1.5-5.0 times uniaxially and then oriented 2.5-5.0 times in the direction perpendicularly intersection to the uniaxial direction so as to be gradually formed into a biaxially oriented film, and a heat treatment at 60-130 deg.C for 0.01-60 seconds is applied to the film. Thus, the film is prepared in such manner that the degree of face orientation (DELTAP) of the film is in the range of 0.070-0.150 on both surfaces of the film and the rate of shrinkage after treatment in 97 deg.C hot water for 30 seconds is 15-50% in one direction and the rate of shrinkage in the direction perpendicularly intersecting to the one direction is somewhat smaller than the former rate, i.e., 5-30% and the tear strength is 700g/mm or over.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は蛍光灯収縮包装用二軸延伸ポリエステルフィル
ムに関するものである。詳しくは本発明は蛍光灯の破損
時におけるガラス破片の飛散防止性能に優れ、収縮包装
時の外観が美しく、均一な透明度を有し、また、耐熱性
に優れた蛍光灯収縮包装用として好適である二軸延伸ポ
リエステルフィルムに関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a biaxially oriented polyester film for shrink wrapping fluorescent lamps. Specifically, the present invention has excellent performance in preventing glass fragments from scattering when fluorescent lamps are broken, has a beautiful appearance when shrink-wrapped, has uniform transparency, and is suitable for shrink-wrapping fluorescent lamps with excellent heat resistance. The present invention relates to a certain biaxially oriented polyester film.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者らは、上記課題に鑑み、鋭意検討した結果、あ
る特定の物性を有する二軸延伸ポリエステルフィルムが
蛍光灯収縮包装用フィルムとして、優れた特性を有する
ことを見出し、本発明を完威するに至った. すなわち本発明の要旨は、フィルムの面配向度(ΔP)
が両面とも0. 0 7 0〜0. 1 5 0の範囲
であり、97℃の熱水中で30秒間処理後の収縮率が一
方向において15〜50%であり、該方向と直交する方
向の収縮率が前記方向の収縮率以下で且つ5〜30%で
あり、且つ引裂強度が700g/閣以上であることを特
徴とする蛍光灯収縮包装用ポリエステルフィルムに存す
る. 以下、本発明を詳細に説明する. 本発明におけるポリエステルは、ジカルボン酸或分とし
て、テレフタル酸、シェウ酸、マロン酸、コハク酸、ア
ジピン酸、アゼライン酸、セバシン酸、フタル酸、イソ
フタル酸、ナフタレンジカルボン酸、ジフェニルエーテ
ルジカルボン酸等、公知のジカルボン酸の一種もしくは
二種以上からなり、また、ジオール威分としてエチレン
グリコール、ネオベンチルグリコール、プロピレングリ
コール、1,4−ブタンジオール、トリメチレングリコ
ール、テトラメチレングリコール、ヘキサメチレングリ
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ノール等公知のジ
オール或分の一種又は二種以上からなるいかなるポリエ
ステル又は共重合ポリエステルであってもよい。
In view of the above-mentioned problems, the present inventors have made extensive studies and found that a biaxially oriented polyester film having certain physical properties has excellent properties as a film for shrink-wrapping fluorescent lamps, and has completed the present invention. I ended up doing it. In other words, the gist of the present invention is to improve the plane orientation degree (ΔP) of the film.
is 0 on both sides. 0 7 0~0. 150, and the shrinkage rate after treatment in hot water at 97°C for 30 seconds is 15 to 50% in one direction, and the shrinkage rate in the direction perpendicular to that direction is less than or equal to the shrinkage rate in the above direction. The present invention provides a polyester film for shrink-wrapping fluorescent lamps, characterized in that the polyester film is 5 to 30% and has a tear strength of 700 g/wall or more. The present invention will be explained in detail below. The polyester in the present invention may be a dicarboxylic acid such as terephthalic acid, schelaic acid, malonic acid, succinic acid, adipic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, naphthalene dicarboxylic acid, diphenyl ether dicarboxylic acid, etc. Consisting of one or more dicarboxylic acids, and diol ingredients such as ethylene glycol, neobentyl glycol, propylene glycol, 1,4-butanediol, trimethylene glycol, tetramethylene glycol, hexamethylene glycol, diethylene glycol, polyethylene glycol, etc. Any polyester or copolyester consisting of one or more types of known diols such as alkylene glycol and 1,4-cyclohexanedimethanol may be used.

共重合戒分としては、ジカルボン酸戒分にイソフタル酸
、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、ジオール戒分に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
、必要に応じて1.  4−シクロヘキサンジメタノー
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、且つ収縮特性も良好で好ましい. 本発明のフィルムは、特に上記共重合ポリエステル威分
を含有することが好ましい。共重合ポリエステル威分の
含有量は、好ましくは、3〜50モル%の範囲であり、
更に好ましくは5〜40モル%、特に好ましくは7〜3
0モル%の範囲である.共重合ポリエステル威分の含有
量が3モル%未満では収縮加工時、フィルムにシワ、歪
み等が発生し、好ましくない。一方、共重合ポリエステ
ル威分の含有量が50モル%を越える場合、フィルムの
強度、耐溶剤性が劣るので好ましくない.また、上記ポ
リエステルは、該ポリエステル以外に30wt%以下で
あれば他のボリマーを添加,混合したものでもよい. 更に、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く、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
化アル逅ニウム、酸化チタン、リン酸カルシウム、フフ
化リチウム、カーボンプ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、架橋ボリマー及びポリエステル合威時に使
用する金属化合物触媒、たと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、ボリマー内部に形威される内部粒子を挙げること
ができる。
Copolymerization ingredients include isophthalic acid, phthalic acid, adipic acid, sebacic acid, and 1,10-decanedicarboxylic acid as dicarboxylic acid ingredients, and neopentyl glycol, diethylene glycol, and polyalkylene glycol as diol ingredients, as necessary. 1. A copolyester using 4-cyclohexanedimethanol is preferred because it is industrially available at low cost and has good shrinkage characteristics. It is particularly preferable that the film of the present invention contains the above-mentioned copolyester component. The content of the copolymerized polyester component is preferably in the range of 3 to 50 mol%,
More preferably 5 to 40 mol%, particularly preferably 7 to 3
The range is 0 mol%. If the content of the copolymerized polyester component is less than 3 mol %, wrinkles, distortions, etc. will occur in the film during shrink processing, which is not preferable. On the other hand, if the content of the copolymerized polyester component exceeds 50 mol%, it is not preferable because the strength and solvent resistance of the film will be poor. Further, the above-mentioned polyester may be one in which other polymers are added or mixed in addition to the polyester, as long as it is not more than 30 wt%. Furthermore, in order to improve the slipperiness of the film, it is preferable to include fine particles such as organic lubricants and inorganic lubricants, and if necessary, stabilizers, colorants, antioxidants, antifoaming agents, and antistatic agents may be added. It may also contain additives such as agents. 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, carbon plaque, and polyester resin. Insoluble high melting point organic compounds during melt film formation, crosslinked polymers and metal compound catalysts used during polyester synthesis, such as alkali metal compounds,
Mention may be made of internal particles formed inside the polymer during polyester production by alkaline earth metal compounds and the like.

フィルム中の微粒子含有量は通常0. 0 0 5〜0
.9重量%の範囲であり、平均粒径は通常0. O O
 1〜3.5μmの範囲である. 本発明においてフィルムの融解熱は好ましくは1 〜8
 cal/ g ,更に好ましくは2〜6cal/gの
範囲である.フィルムの融解熱がlcal/g未満のも
のでは押出製膜前の乾燥工程で、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、該融解熱が8cal/g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. 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0.6
5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 fine particle content in the film is usually 0. 0 0 5~0
.. 9% by weight, and the average particle size is usually 0.9% by weight. O O
It is in the range of 1 to 3.5 μm. In the present invention, the heat of fusion of the film is preferably 1 to 8.
cal/g, more preferably in the range of 2 to 6 cal/g. If the heat of fusion of the film is less than lcal/g, it will be difficult to use the drying method normally used for polyethylene terephthalate in the drying process before extrusion film formation, which is undesirable. Further, a film having a heat of fusion exceeding 8 cal/g is not preferable because a sufficient shrinkage rate cannot be obtained. The intrinsic viscosity of the film of the present invention is preferably 0.50 or more, more preferably 0.60 or more, particularly preferably 0.6
It is 5 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.

本発明のフィルムにおいて97℃の熱水中で30秒間処
理後の収縮率がフィルムの一方向(以下、主収縮方向と
称する)において15〜50%の範囲であることが必要
であり、好ましくは17〜45%、更に好ましくは20
〜40%の範囲である。
In the film of the present invention, it is necessary that the shrinkage rate after treatment in hot water at 97°C for 30 seconds is in the range of 15 to 50% in one direction of the film (hereinafter referred to as the main shrinkage direction), and preferably 17-45%, more preferably 20
~40% range.

フィルムの主収縮方向の収縮率が15%未満の場合、収
縮加工時、収縮量が不十分となり、フィルムが蛍光灯に
十分密着せず不適当である。またフィルムの主収縮方向
の収縮率が50%を越すフィルムでは、収縮加工時、フ
ィルムにシワ、歪み等が発生し、不適当である. 本発明のフィルムの主収縮方向と直交する方向の97℃
の熱水中で30秒間処理後の収縮率は主収縮方向の収縮
率以下であり且つ5〜30%の範囲であることが必要で
あり、好ましくは主収縮方向の収縮率以下で且つ7〜2
5%、更に好ましくは主収縮方向の収縮率以下で且つ1
0〜20%の範囲である。
If the shrinkage rate of the film in the main shrinkage direction is less than 15%, the amount of shrinkage will be insufficient during shrinkage processing, and the film will not adhere sufficiently to the fluorescent lamp, which is inappropriate. Furthermore, if the shrinkage rate in the main shrinkage direction of the film exceeds 50%, wrinkles, distortions, etc. will occur in the film during shrinkage processing, making it unsuitable. 97°C in a direction perpendicular to the main shrinkage direction of the film of the present invention
The shrinkage rate after treatment in hot water for 30 seconds must be less than the shrinkage rate in the main shrinkage direction and in the range of 5 to 30%, preferably less than the shrinkage rate in the main shrinkage direction and in the range of 7 to 30%. 2
5%, more preferably shrinkage rate in the main shrinkage direction or less and 1
It is in the range of 0-20%.

かかる収縮率が5%未満の場合には、収縮包装時に、収
縮量が不十分であり、蛍光灯の端の部分がうまく包み込
めず加工性に劣るため不適当である。また主収縮方向と
直交する方向の収縮率が30%を越す場合には、収縮包
装時に、蛍光灯の長手方向の収縮量が大き過ぎ、蛍光灯
の長手方向に収縮後のフィルムの寸法が合わなくなるた
め不適当である。
If the shrinkage rate is less than 5%, the amount of shrinkage will be insufficient during shrink wrapping, and the ends of the fluorescent lamp will not be wrapped well, resulting in poor processability, which is unsuitable. If the shrinkage rate in the direction perpendicular to the main shrinkage direction exceeds 30%, the amount of shrinkage in the longitudinal direction of the fluorescent lamp is too large during shrink wrapping, and the dimensions of the shrunk film will not match the longitudinal direction of the fluorescent lamp. It is inappropriate because it will disappear.

また、本発明のフィルムにおいて、主収縮方向の収縮率
(αl)、主収縮方向と直交する収縮率(α2)との比
、α1/α2は1. l〜5.0の範囲であることが好
ましく、1.2〜4. 0の範囲が更に好ましく、1.
 3〜3.5の範囲が特に好ましい.α1/α2が1.
1未満である場合、収縮包装時にフィルムにシワ、歪み
等が発生し好ましくない.一方、本発明のフィルムにお
いてαl/α2が5.0を越す場合、収縮包装時に螢光
灯の端の部分がうまく包み込めず加工性に劣るため好ま
しくない。
Further, in the film of the present invention, the ratio of the shrinkage rate (αl) in the main shrinkage direction to the shrinkage rate (α2) perpendicular to the main shrinkage direction, α1/α2, is 1. It is preferably in the range of 1 to 5.0, and 1.2 to 4. A range of 0 is more preferable, and 1.
A range of 3 to 3.5 is particularly preferred. α1/α2 is 1.
If it is less than 1, wrinkles, distortions, etc. will occur in the film during shrink wrapping, which is undesirable. On the other hand, if αl/α2 exceeds 5.0 in the film of the present invention, it is not preferable because the end portion of the fluorescent lamp cannot be wrapped well during shrink wrapping, resulting in poor processability.

更に、本発明のフィルムの引裂強度は700g/一以上
であることが必要である.好ましくは1000g/al
l以上、更に好ましくは1500g/閣以上である. フィルムの引裂強度が700g/III未満の場合には
、飛散防止膜としての機能が十分でなくなるために不適
当である. 本発明のフィルムの面配向度(ΔP)は両面とも0. 
0 7 0〜0. 1 5 0の範囲であることが必要
であり、好ましくは0.0 8 0 −0. 1 4 
0、更に好ましくは0. 0 8 5〜0. 1 3 
0の範囲である.ΔPが0. 0 7 0未満の場合、
収縮包装フィルムの飛散防止性が十分でなくなるため不
適当である.一方、ΔPが0. 1 5 0を越す場合
には収縮加工詩、フイルムにシワ、歪み等が発生するた
め不適当である.また、本発明においてフィルムの片面
側の面配向度(ΔP,)とその反対面側の面配向度(Δ
P2)の相対差すなわち、1ΔP1−Δp.Iは、0.
 0 5 0以下であることが好ましい.更に好ましく
は0. 0 4 0以下であり、特に好ましくは0.0
20以下である。1ΔP1−Δpg  Iが0. 0 
5 0を越す場合には収縮加工時、フィルムにシワ、歪
み等が発生したり、蛍光灯の破損時における飛散防止性
が十分でなくなるため好ましくない。
Furthermore, it is necessary that the tear strength of the film of the present invention is 700 g/1 or more. Preferably 1000g/al
1 or more, more preferably 1500g/kil or more. If the tear strength of the film is less than 700 g/III, it is unsuitable because its function as a scattering prevention film will not be sufficient. The plane orientation degree (ΔP) of the film of the present invention is 0.0 on both sides.
0 7 0~0. It needs to be in the range of 150, preferably 0.080-0. 1 4
0, more preferably 0. 0 8 5~0. 1 3
The range is 0. ΔP is 0. 0 7 If less than 0,
This is unsuitable because the shatterproof properties of the shrink wrapping film will not be sufficient. On the other hand, ΔP is 0. If it exceeds 150, it is not suitable because it will cause shrinkage, wrinkles, distortion, etc. on the film. In addition, in the present invention, the degree of plane orientation (ΔP,) on one side of the film and the degree of plane orientation (ΔP,) on the opposite side of the film are also determined.
P2), that is, 1ΔP1−Δp. I is 0.
It is preferable that it is 0.5 or less. More preferably 0. 0 4 0 or less, particularly preferably 0.0
20 or less. 1ΔP1−Δpg I is 0. 0
If it exceeds 50, wrinkles, distortions, etc. will occur in the film during shrinkage processing, and the shatterproof property will not be sufficient when the fluorescent lamp is damaged, which is not preferable.

本発明のフィルムの長手方向の厚さ斑は、30%以下が
好ましい。更に好ましくは25%以下、特に好ましくは
20%以下である。フィルムの厚さ斑が30%を越える
場合、収縮加工時にフィルムにシワ、歪み等が発生した
りフィルムの透明度が不均一になり、包装した蛍光灯の
外観が損われるだけでなく、蛍光灯を点灯した際の照射
光の強度が不均一になるため好ましくない. 本発明のフィルムのヘーズ値は10%以下が好ましく、
更に好ましくは7%以下、特に好ましくは5%以下であ
る。ヘーズ値がlO%を越えると蛍光灯を点灯した際の
照射光の強度が弱くなるので好ましくない. なお、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塑性
樹脂のフィルム、又はシートを積層してクッション性を
持たせ、蛍光灯の破損時における破片の飛散防止性能を
更に高めることも可能である。そのような熱可塑性樹脂
としてはポリ塩化ビニル、ポリエチレン、ボリブロピレ
ン、ポリアクリル系、ボリスチレン、ポリエステル等、
既知のいかなる熱可塑性樹脂も用いられる.次に本発明
のフィルムの製造法を具体的に説明するが、本発明はそ
の要旨を越えない限り下記製造法に特に限定されるもの
ではない。
The thickness unevenness in the longitudinal direction of the film of the present invention is preferably 30% or less. It is more preferably 25% or less, particularly preferably 20% or less. If the thickness unevenness of the film exceeds 30%, wrinkles and distortions may occur in the film during shrinkage processing, and the transparency of the film may become uneven, which not only impairs the appearance of the packaged fluorescent lamp, but also makes it difficult to use the fluorescent lamp. This is not desirable because the intensity of the irradiated light becomes uneven when the light is turned on. The haze value of the film of the present invention is preferably 10% or less,
More preferably it is 7% or less, particularly preferably 5% or less. If the haze value exceeds 10%, the intensity of the irradiated light will be weakened when the fluorescent lamp is turned on, which is not preferable. In addition, a foaming ink layer is printed on one or both sides of the film of the present invention, or a thermoplastic resin film or sheet with bubbles inside is laminated to provide cushioning properties, so that it can be used in the event of damage to a fluorescent lamp. It is also possible to further improve the performance of preventing scattering of fragments. Such thermoplastic resins include polyvinyl chloride, polyethylene, polypropylene, polyacrylic, polystyrene, polyester, etc.
Any known thermoplastic resin can be used. Next, the method for producing the film of the present invention will be specifically explained, but the present invention is not particularly limited to the following production method unless it exceeds the gist thereof.

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
エステル又は共重合ポリエステルを、通常のホッパドラ
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℃の温度で押出しを行なう. 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用い
ることにより厚さ斑の均一なフィルムを得ることができ
る。
Polyester or copolyester containing an appropriate amount of inorganic particles as a lubricant, if necessary, is dried using an ordinary hopper dryer, paddle dryer, vacuum dryer, etc., and then extruded at a temperature of 200 to 320°C. After extrusion, the film is rapidly cooled to obtain an unstretched film. When the T-die method is used, a film with uniform thickness can be obtained by using a so-called electrostatic application adhesion method during the rapid cooling.

このようにして得た未延伸フィルムは、まず一軸方向(
通常は縦方向)に1.5〜5.0倍延伸し、次に該方向
と直交する方向に2.5〜5. 0倍延伸し逐次二軸延
伸フィルムとする. このようにして延伸されたフィルムは、60〜130℃
で0.Ol〜60秒の熱処理が施される.熱処理は通常
、緊張固定下実施されるが、同時に20%以下の弛緩又
は巾出しを行な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
把持して行な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なうことも可能である。
The unstretched film obtained in this way is first uniaxially (
Stretched 1.5 to 5.0 times in the longitudinal direction (usually the longitudinal direction), then 2.5 to 5.0 times in the direction perpendicular to the longitudinal direction. Stretch 0 times to make a sequentially biaxially stretched film. The film stretched in this way has a temperature of 60 to 130°C.
So 0. Heat treatment is performed for 60 seconds. Heat treatment is usually carried out under tension fixation, but it is also possible to loosen or widen the material by 20% or less at the same time. As the heat treatment method, known methods such as a method in which the material is brought into contact with a heating roll or a method in which the material is gripped by 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、又は延伸後にフィルム
の片面又は両面に塗布を行ない、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。
It is also possible to improve the adhesion, antistatic properties, slipperiness, light-shielding properties, etc. of the film by coating one or both sides of the film during, before, or after the stretching process.

かくして得られたフィルムを巻き取り、製品とする. 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、蛍光灯収縮包装用フィルムとして好ましく用
いられる厚さとしてはlO〜300μmの範囲であり、
特に好ましくは20〜200μmの範囲である. 〔実施例〕 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越えない限り、これらの実施例に限
定されるものではない.なお、フィルムの評価方法を以
下に示す.(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7=50
750の混合溶媒20mj!に加え、約110℃で1時
間加熱後、30℃で測定した.(2)面配向度(ΔP) アタゴ■製アッペの屈折計を使用し、光源にはナトリウ
ムランプを用いて測定した.なお、測定はフィルム両面
について行なった。
The film thus obtained is rolled up and made into a product. The thickness of the film obtained as described above is not particularly limited, but the thickness preferably used as a shrink wrapping film for fluorescent lamps is in the range of 10 to 300 μm,
Particularly preferred is a range of 20 to 200 μm. [Example] 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 goes beyond the gist thereof. The method for evaluating the film is shown below. (1) Intrinsic viscosity of film [η] Sample 200cm was mixed with phenol/tetrachloroethyl 7=50
750 mixed solvent 20mj! In addition, the temperature was measured at 30°C after heating at about 110°C for 1 hour. (2) Degree of planar orientation (ΔP) Measurement was performed using an Appe refractometer manufactured by Atago ■ and a sodium lamp as the light source. Note that the measurements were performed on both sides of the film.

フィルム面内の最大の屈折率n7、それに直角方向の屈
折率nβ、及び厚さ方向の屈折率nαを求め、面配向度
を算出した. 2 (3)収縮率 無張力状態で、97℃の熱水中で30秒間熱処理し、そ
の前後のフィルムの長さを測定することにより次式にて
計算した. (4)へーズ JIS  K6714に準じ、日本電色工業社製分球式
濁度計NDH−200によりフィルムのヘーズ値を測定
した. (5)引裂強度(g/閣) 輻50m長さ63.5鵬のASTM  D1922記載
の方法に準じ、東洋精機製作所■製軽荷重引裂試験機を
用いて試料フィルムを50■引裂くのに要する荷重を測
定し、フィルム厚さ(Infll)で除し引裂強度とし
た. (6)フィルムの収縮特性(シワ、歪み及び加工性)試
料フィルムの主収縮方向を蛍光灯の径方向に沿うように
して試料フィルムを巻き、接着剤を用いて直径34mの
円筒形に製袋した後、蛍光灯に被せ、シュリンクトンネ
ルを通過させ収縮させた.収縮包装の仕上りの評価とし
てシワ、歪みについて視覚により○,Δ,×で判定した
。○は各々の欠点がほとんど見られないもの、Δは欠点
が若干見られるものの実用化可能なもの、×は数多く欠
点が見られ実用化に耐えられないものとした。
The maximum refractive index n7 in the film plane, the refractive index nβ in the direction perpendicular to it, and the refractive index nα in the thickness direction were determined, and the degree of plane orientation was calculated. 2 (3) Shrinkage rate The shrinkage rate was calculated using the following formula by heat-treating the film in hot water at 97°C for 30 seconds under no tension and measuring the length of the film before and after the treatment. (4) Haze The haze value of the film was measured according to JIS K6714 using a sphere-splitting turbidity meter NDH-200 manufactured by Nippon Denshoku Industries. (5) Tear strength (g/kaku) Required to tear a sample film for 50 mm using a light load tear tester manufactured by Toyo Seiki Co., Ltd. according to the method described in ASTM D1922 with a diameter of 50 m and a length of 63.5 mm. The load was measured and divided by the film thickness (Inflll) to obtain the tear strength. (6) Shrinkage characteristics of the film (wrinkles, distortion, and workability) The sample film was wound so that its main shrinkage direction was along the radial direction of the fluorescent lamp, and made into a cylindrical bag with a diameter of 34 m using adhesive. After that, it was placed over a fluorescent light and passed through a shrink tunnel to shrink. To evaluate the finish of the shrink wrap, wrinkles and distortion were visually judged as ○, Δ, and ×. ○ indicates that almost no defects are observed, Δ indicates that some defects are observed but can be put into practical use, and × indicates that many defects are observed and cannot be put into practical use.

また、加工性の評価として、次のように判定した.○は
蛍光灯の端の部分がうまく包み込まれているもの、×は
蛍光灯の端の部分がうまく包み込まれていないものとし
た. (7)落下時飛散テスト 試料フィルムを収縮包装した蛍光灯を2.0mの高さか
ら床に落下させた後、ガラスの破片が飛散した距離によ
り次のように評価した. また、上記の評価項目(7). (8). (9)を総
合的に考慮し、○,×の総合評価を与えた. 実施例1 ジカルボン酸戒分としてテレフタル酸841101%、
イソフタル酸単位1 5 mol%よりなり、ジオール
戒分としてエチレングリコール単位よりなる、平均粒径
1. 3μmの無定形シリカ300ppmを含む〔η)
=0.71の共重合ポリエステルを120℃、4時間で
予備結晶化後、l80″C、4時間の乾燥を行ない、そ
の後押出機で290℃に溶融後Tダイより押出し急冷固
化して未延伸シートを得た. 該未延伸シートを85℃の加熱ロールにより縦方向に3
.2倍延伸した後、テンターに導き横方向に90℃で3
.6倍延伸を行ない、続いて105℃で熱処理を行ない
さらに冷却後巻き取り、平均厚さ100unの逐次二輪
延伸フイルムを得た。
In addition, the workability was evaluated as follows. ○ indicates that the end of the fluorescent light is wrapped well, and × means that the end of the fluorescent light is not wrapped well. (7) Drop scattering test After dropping a fluorescent lamp shrink-wrapped sample film onto the floor from a height of 2.0 m, the following evaluation was made based on the distance that glass fragments were scattered. In addition, the above evaluation item (7). (8). Considering (9) comprehensively, we gave an overall evaluation of ○ or ×. Example 1 Terephthalic acid 841101% as dicarboxylic acid component,
The average particle size is 1.5 mol% of isophthalic acid units and ethylene glycol units as the diol component. Contains 300 ppm of 3 μm amorphous silica [η)
=0.71 copolymerized polyester was pre-crystallized at 120°C for 4 hours, dried at 180''C for 4 hours, then melted at 290°C with an extruder, extruded through a T-die, rapidly solidified, and unstretched. A sheet was obtained. The unstretched sheet was rolled 3 times in the longitudinal direction using a heated roll at 85°C.
.. After stretching 2 times, it is introduced into a tenter and stretched at 90°C for 3 times in the transverse direction.
.. Stretching was performed 6 times, followed by heat treatment at 105° C., and after cooling, the film was wound up to obtain a sequentially stretched two-wheel film having an average thickness of 100 um.

実施例2 ジカルボン酸戒分としてテレフタル酸単位よりなり、ジ
オール或分としてエチレングリコール単位82.5mo
l%、ネオペンチルグリコール単位12.5mol%、
ジエチレングリコーノレ単位5−Ol%よりなる、〔η
)=0.65の共重合ポリエステルと、平均粒径1.0
μmの無定形シリカ1000ppmを含む(η)=0.
70のポリエチレルテレフタレートを重量比6 0/4
 0の割合でブレンド後、実施例1と全く同様に乾燥、
押出し、急冷固化して未延伸シートを得た. 該未延伸シートを85℃の加熱ロールにより縦方向に3
.2倍延伸した後、テンターに導き横方向に90℃で3
.6倍延伸を行ない、続いて95℃で熱処理を行ない、
冷却後巻き取り、平均厚さ100μmの逐次二軸延伸フ
ィルムを得た. 比較例l 実施例1の未延伸シートを直接テンターに導き横方向に
90℃で3.0倍延伸し、続いて105℃で熱処理を行
ない、冷却後巻き取り平均厚さ100μmの一軸延伸フ
ィルムを得た. 比較例2 ジカルボン酸成分としてテレフタル酸8411101%
、イソフタル酸単位l6IlO1%よりなり、ジオール
或分としてエチレングリコール単位よりなる、平均粒径
7.5μmの無定形シリカ1000ppmを含む〔η)
−0.70の共重合ポリエステルを常法にて乾燥し、そ
の後押出機で285℃に溶融後環状ダイスより押出し、
冷却して管状の未延伸シートを得た. 該管状の未延伸シートの端末から加圧気体を注入し、9
0℃設定にて径方向に3.6倍膨張させると同時にディ
ファレンシャルスピードロールによって軸方向にも3.
1倍延伸し、続いて105℃で熱処理を行ない、冷却後
巻き取り、平均厚さ100μmのチューブラ法同時二輪
延伸フィルムを得た。
Example 2 Consisting of terephthalic acid units as the dicarboxylic acid component and 82.5 mo of ethylene glycol units as the diol component
l%, neopentyl glycol units 12.5 mol%,
Consisting of 5-Ol% diethylene glycol units, [η
) = 0.65 copolymerized polyester and average particle size 1.0
Contains 1000 ppm of μm amorphous silica (η)=0.
70 polyethylene terephthalate at a weight ratio of 60/4
After blending at a ratio of 0, dry in exactly the same manner as in Example 1,
An unstretched sheet was obtained by extrusion and rapid solidification. The unstretched sheet was rolled in the longitudinal direction by heating rolls at 85°C.
.. After stretching 2 times, it is introduced into a tenter and stretched at 90°C for 3 times in the transverse direction.
.. Stretched 6 times, followed by heat treatment at 95°C,
After cooling, the film was wound up to obtain a sequentially biaxially stretched film with an average thickness of 100 μm. Comparative Example 1 The unstretched sheet of Example 1 was directly introduced into a tenter and stretched 3.0 times in the transverse direction at 90°C, followed by heat treatment at 105°C, and after cooling, it was rolled up to form a uniaxially stretched film with an average thickness of 100 μm. Obtained. Comparative Example 2 Terephthalic acid 8411101% as dicarboxylic acid component
, containing 1000 ppm of amorphous silica with an average particle size of 7.5 μm, consisting of 1% of isophthalic acid units l6IlO and ethylene glycol units as diol part [η)
-0.70 copolymerized polyester was dried in a conventional manner, then melted at 285°C in an extruder and extruded through an annular die.
After cooling, a tubular unstretched sheet was obtained. Pressurized gas is injected from the end of the tubular unstretched sheet, and 9
At 0°C setting, it is expanded 3.6 times in the radial direction, and at the same time, it is expanded 3.6 times in the axial direction using a differential speed roll.
The film was stretched once, then heat-treated at 105° C., cooled, and then wound to obtain a two-wheel simultaneous tubular stretched film with an average thickness of 100 μm.

以上、得られた結果をまとめて表−1に示す。The results obtained above are summarized in Table 1.

〔発明の効果〕〔Effect of the invention〕

本発明のフィルムは収縮包装時のフィルムのシワ、歪み
等が極めて少なく、加工性に優れた収縮特性を有し、蛍
光灯の破損時におけるガラス破片の飛散防止性も非常に
優れており、蛍光灯収縮包装用として工業的価値の極め
て高いフィルムである。
The film of the present invention has extremely few wrinkles, distortions, etc. during shrink wrapping, and has excellent shrinkage characteristics that make it easy to process.It also has excellent properties to prevent glass fragments from scattering when a fluorescent lamp is broken, and This is a film with extremely high industrial value for use in light shrink packaging.

Claims (1)

【特許請求の範囲】[Claims] (1)フィルムの面配向度(ΔP)が両面とも0.07
0〜0.150の範囲であり、97℃の熱水中で30秒
間処理後の収縮率が一方向において15〜50%であり
、該方向と直交する方向の収縮率が前記方向の収縮率以
下で且つ5〜30%であり、且つ引裂強度が700g/
mm以上であることを特徴とする蛍光灯収縮包装用ポリ
エステルフィルム。
(1) The plane orientation degree (ΔP) of the film is 0.07 on both sides.
0 to 0.150, and the shrinkage rate after treatment in 97°C hot water for 30 seconds is 15 to 50% in one direction, and the shrinkage rate in the direction perpendicular to the said direction is the shrinkage rate in the said direction. or less and 5 to 30%, and the tear strength is 700g/
A polyester film for shrink-wrapping fluorescent lamps, which is characterized by having a film size of 1 mm or more.
JP15259389A 1989-06-15 1989-06-15 Polyester film for fluorescent light shrink packaging Expired - Fee Related JP2692270B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15259389A JP2692270B2 (en) 1989-06-15 1989-06-15 Polyester film for fluorescent light shrink packaging

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15259389A JP2692270B2 (en) 1989-06-15 1989-06-15 Polyester film for fluorescent light shrink packaging

Publications (2)

Publication Number Publication Date
JPH0329763A true JPH0329763A (en) 1991-02-07
JP2692270B2 JP2692270B2 (en) 1997-12-17

Family

ID=15543829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15259389A Expired - Fee Related JP2692270B2 (en) 1989-06-15 1989-06-15 Polyester film for fluorescent light shrink packaging

Country Status (1)

Country Link
JP (1) JP2692270B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05245930A (en) * 1991-12-26 1993-09-24 Sekisui Chem Co Ltd Polyester heat-shrinkable film
JPH05318587A (en) * 1992-05-21 1993-12-03 Toyobo Co Ltd Heat shrinkable polyester series film
JPH06321253A (en) * 1993-05-06 1994-11-22 Okura Ind Co Ltd Film for bandage type sleeve wrap, and usage thereof
JPH08192464A (en) * 1995-01-19 1996-07-30 Kanebo Ltd Polyester heat-shrinkable film
WO2002087853A1 (en) * 2001-04-26 2002-11-07 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester film roll and process for producing the same
WO2003039841A1 (en) * 2001-08-01 2003-05-15 Toyo Boseki Kabushiki Kaisha Heat shrinking polyester film roll
EP1441000A2 (en) 1998-01-30 2004-07-28 Toyo Boseki Kabushiki Kaisha Thermo-shrinkable polyester film

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05245930A (en) * 1991-12-26 1993-09-24 Sekisui Chem Co Ltd Polyester heat-shrinkable film
JPH05318587A (en) * 1992-05-21 1993-12-03 Toyobo Co Ltd Heat shrinkable polyester series film
JPH06321253A (en) * 1993-05-06 1994-11-22 Okura Ind Co Ltd Film for bandage type sleeve wrap, and usage thereof
JPH08192464A (en) * 1995-01-19 1996-07-30 Kanebo Ltd Polyester heat-shrinkable film
EP1441000A2 (en) 1998-01-30 2004-07-28 Toyo Boseki Kabushiki Kaisha Thermo-shrinkable polyester film
WO2002087853A1 (en) * 2001-04-26 2002-11-07 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester film roll and process for producing the same
US7939174B2 (en) 2001-04-26 2011-05-10 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester film roll and a process for producing the same
WO2003039841A1 (en) * 2001-08-01 2003-05-15 Toyo Boseki Kabushiki Kaisha Heat shrinking polyester film roll

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