JP2003145695A - Method for manufacturing polyethylenic heat-shrinkable film - Google Patents
Method for manufacturing polyethylenic heat-shrinkable filmInfo
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- JP2003145695A JP2003145695A JP2001344137A JP2001344137A JP2003145695A JP 2003145695 A JP2003145695 A JP 2003145695A JP 2001344137 A JP2001344137 A JP 2001344137A JP 2001344137 A JP2001344137 A JP 2001344137A JP 2003145695 A JP2003145695 A JP 2003145695A
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Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、DVDやビデオの
包装に用いられる、ポリエチレン系低温熱収縮フィルム
に関するものであり、低温収縮性に優れ、特に角や辺に
シワの入らない、包装仕上がりの良いポリエチレン系低
温熱収縮フィルム及びその製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyethylene-based low-temperature heat-shrinkable film used for packaging DVDs and videos, which has excellent low-temperature shrinkability, and has no wrinkles on corners or sides, and has a finished package. It relates to a good polyethylene-based low temperature heat-shrinkable film and a manufacturing method thereof.
【0002】[0002]
【従来の技術】従来DVDやビデオソフトの包装には、
収縮温度範囲が広く作業性が良い、角や辺にシワがなく
包装仕上がりが良い等の理由で、ポリ塩化ビニル系シュ
リンクフィルムが用いられてきた。しかしながら熱シー
ル性が良くない、臭いがする等の品質問題、ダイオキシ
ン等の環境問題があり、ポリ塩化ビニル系シュリンクフ
ィルム代替品として熱収縮性が良く、低コストで、環境
問題もない、ポリエチレン等のポリオレフィンフィルム
を使用したいという要望が強い。そこで、例えば内外層
にポリプロピレン系樹脂、芯層にポリエチレン系樹脂を
使用し2軸延伸したフィルム、内外層にポリオレフィン
系樹脂、芯層に内外層よりも密度の低いポリオレフィン
系樹脂を使用し架橋後延伸したフィルム、内外層にポリ
エチレン系樹脂、芯層にエチレン・酢酸ビニルコポリマ
ーを使用し架橋延伸したフィルム等が開発されている。2. Description of the Related Art Conventionally, packaging of DVDs and video software has been
Polyvinyl chloride-based shrink films have been used because of their wide shrinkage temperature range, good workability, no wrinkles on the corners and sides, and good packaging finish. However, it does not have good heat-sealing properties, there are quality problems such as smelling, environmental problems such as dioxins, and it has good heat shrinkability as a substitute for polyvinyl chloride shrink film, low cost, no environmental problems, polyethylene, etc. There is a strong desire to use the above polyolefin film. Therefore, for example, a polypropylene resin is used for the inner and outer layers, a polyethylene resin is used for the core layer, and a biaxially stretched film is used, a polyolefin resin is used for the inner and outer layers, and a polyolefin resin with a lower density than the inner and outer layers is used for the core layer, and after crosslinking Stretched films, polyethylene-based resins for the inner and outer layers, and cross-linked stretched films using ethylene / vinyl acetate copolymer for the core layer have been developed.
【0003】しかしながら、これらのフィルム、例えば
内外層にポリプロピレン系樹脂を使用、芯層にポリエチ
レン系樹脂を使用し2軸延伸したフィルムは、熱収縮率
がポリプロピレン系シュリンクフィルムに近く、低温収
縮性が充分でなく、仕上がりが良くない等の欠点があ
る。また、内外層にポリオレフィン系樹脂、芯層に内外
層よりも密度の低いポリオレフィン系樹脂、あるいはエ
チレン・酢酸ビニルコポリマーを使用し架橋後延伸した
フィルムは、低温収縮性は改善されているが、収縮温度
範囲が狭く、溶断カット性が悪い等の欠点がある。However, these films, for example, a biaxially stretched film in which polypropylene resin is used for the inner and outer layers and polyethylene resin is used for the core layer, have a heat shrinkage ratio close to that of the polypropylene shrink film and have low temperature shrinkability. There are drawbacks such as not being sufficient and the finish being poor. In addition, a polyolefin resin for the inner and outer layers, a polyolefin resin having a lower density than the inner and outer layers for the core layer, or a film stretched after crosslinking using ethylene / vinyl acetate copolymer has improved low-temperature shrinkability, but shrinks. It has drawbacks such as narrow temperature range and poor fusing cutability.
【0004】[0004]
【発明が解決しようとする課題】そこで本発明の目的
は、DVDやビデオの包装に用いられ、低温収縮性に優
れ、特に角や辺にシワの入らない、包装仕上がりの良い
ポリエチレン系低温熱収縮フィルムを提供することにあ
る。また、本発明の目的は、収縮温度範囲が広く、溶断
カット性の良いポリエチレン系低温熱収縮フィルムを提
供することにある。Therefore, an object of the present invention is to use polyethylene for low temperature heat shrinkage which is used for packaging DVDs and videos, has excellent low temperature shrinkability, and in particular has no wrinkles on corners and sides and has a good packaging finish. To provide a film. Another object of the present invention is to provide a polyethylene-based low temperature heat-shrinkable film having a wide shrinking temperature range and good melt-cutting property.
【0005】[0005]
【課題を解決するための手段】本発明者らは、これらの
問題を解決するために鋭意研究の結果、芯層に石油樹脂
と、低密度ポリエチレン系樹脂を配合することにより、
これらの問題を解決できることを見出し、本発明をなす
に至った。本発明は、以下の発明を包含する。Means for Solving the Problems As a result of intensive research to solve these problems, the present inventors have found that by blending a petroleum resin and a low density polyethylene resin in the core layer,
The inventors have found that these problems can be solved and have completed the present invention. The present invention includes the following inventions.
【0006】(1)密度0.905〜0.960g/c
m3のポリエチレン系樹脂からなる2つの表面層と、石
油樹脂2〜30質量%、密度0.870〜0.935g
/cm 3のポリエチレン系樹脂98〜70質量%の混合
樹脂からなる芯層を共押出しし、10〜100kGyの
電子線を照射した後、縦及び横方向に3〜10倍に延伸
することを特徴とするポリエチレン系2軸延伸熱収縮フ
ィルムの製造方法。(1) Density 0.905 to 0.960 g / c
m3Two surface layers made of polyethylene resin and stone
Oil resin 2 to 30 mass%, density 0.870 to 0.935g
/ Cm 3Of polyethylene resin 98-70% by mass
A core layer made of resin is co-extruded to obtain 10 to 100 kGy.
After irradiating with an electron beam, stretch in the longitudinal and transverse directions 3 to 10 times
Polyethylene biaxially stretched heat shrinkable film characterized by
Method of manufacturing film.
【0007】(2)芯層のポリエチレン系樹脂は、密度
0.920〜0.935g/cm3のポリエチレン系樹
脂と、密度0.870〜0.915g/cm3のポリエ
チレン系樹脂の混合物である(1)項に記載のポリエチ
レン系2軸延伸熱収縮フィルムの製造方法。(2) The polyethylene resin of the core layer is a mixture of a polyethylene resin having a density of 0.920 to 0.935 g / cm 3 and a polyethylene resin having a density of 0.870 to 0.915 g / cm 3. The method for producing a polyethylene-based biaxially stretched heat-shrinkable film according to item (1).
【0008】本発明は更に以下の発明を包含する。
(3)芯層の密度0.920〜0.935g/cm3の
ポリエチレン系樹脂の割合は、芯層のポリエチレン系樹
脂中の5〜20質量%である(1)項又は(2)項に記
載のポリエチレン系2軸延伸熱収縮フィルムの製造方
法。
(4)石油樹脂を除くポリエチレン系樹脂(表面層と芯
層の合計)の平均密度が0.910g/cm3以下であ
る(1)項〜(3)項のいずれか1項に記載のポリエチ
レン系2軸延伸熱収縮フィルムの製造方法。The present invention further includes the following inventions. (3) The proportion of the polyethylene-based resin having a density of 0.920 to 0.935 g / cm 3 in the core layer is 5 to 20% by mass based on the polyethylene-based resin in the core layer. A method for producing the described polyethylene-based biaxially stretched heat-shrinkable film. (4) The polyethylene according to any one of items (1) to (3), wherein the polyethylene resin (the total of the surface layer and the core layer) excluding petroleum resin has an average density of 0.910 g / cm 3 or less. Method for producing a biaxially stretched heat-shrinkable film.
【0009】(5)上記(1)項〜(4)項のいずれか
1項に記載の方法でつくられたポリエチレン系2軸延伸
熱収縮フィルム。
(6)100℃の加熱収縮率が縦横共35%以上、90
℃の加熱収縮率が縦横共20%以上である(5)項に記
載のポリエチレン系2軸延伸熱収縮フィルム。(5) A polyethylene-based biaxially stretched heat-shrinkable film produced by the method described in any one of the above items (1) to (4). (6) Heat shrinkage at 100 ° C. is 35% or more in both length and width, 90
The polyethylene-based biaxially stretched heat-shrinkable film according to the item (5), which has a heat shrinkage at 20 ° C. of 20% or more in both length and width.
【0010】[0010]
【発明の実施の形態】本発明の熱収縮フィルムの芯層
は、石油樹脂と密度0.870〜0.935g/cm3
のポリエチレン系樹脂の混合樹脂からなる。ここで用い
られる石油樹脂は、脂環族飽和炭化水素のことで、石油
精製時に得られるC9留分の重合物を水添して得られ
る。石油樹脂は主に製膜性安定のために使用される。D
VD包装時の良好な仕上がりを得るためには、低温での
熱収縮率を大きくする必要があるが、この目的のために
通常融点が110℃以下の低融点のポリエチレンが使用
される。しかしながら低融点になればなるほど製膜が安
定せず、延伸は不可能になるが、石油樹脂を適量添加す
ることにより、安定した製膜が可能になる。BEST MODE FOR CARRYING OUT THE INVENTION The core layer of the heat shrinkable film of the present invention comprises petroleum resin and a density of 0.870 to 0.935 g / cm 3.
It is made of a mixed resin of polyethylene resin. The petroleum resin used here is an alicyclic saturated hydrocarbon, and is obtained by hydrogenating a polymer of a C9 fraction obtained during petroleum refining. Petroleum resin is mainly used for stabilizing the film-forming property. D
In order to obtain a good finish in VD packaging, it is necessary to increase the heat shrinkage rate at low temperatures, but for this purpose, polyethylene having a low melting point of 110 ° C. or lower is usually used. However, the lower the melting point, the more unstable the film formation and the inability to stretch. However, by adding an appropriate amount of petroleum resin, stable film formation becomes possible.
【0011】また、石油樹脂添加により、フィルムの腰
を強くすることができる。ポリエチレンを主たる原料と
しているフィルムは腰が弱く、包装時の作業性がポリプ
ロプレン系フィルムと比較して劣っているが、本発明の
ように石油樹脂を添加することで腰が強くなり、包装時
の作業性が改善される。もう一つの石油樹脂添加の利点
は、フィルムの透明性向上である。DVDは店頭で直接
消費者の目に触れるため、透明度、光沢度の向上は重要
である。The addition of petroleum resin can strengthen the rigidity of the film. The film made mainly of polyethylene has a low rigidity and is inferior in workability at the time of packaging as compared with the polypropylene-based film, but by adding a petroleum resin as in the present invention, the rigidity becomes strong and Workability is improved. Another advantage of adding a petroleum resin is improving the transparency of the film. Since DVDs are directly exposed to consumers at stores, it is important to improve transparency and gloss.
【0012】芯層中の石油樹脂の配合量は2〜30質量
%、好ましくは10〜20質量%である。石油樹脂の配
合量が2質量%に満たない場合、延伸点が変動し、製膜
が安定しないばかりでなく、フィルムの偏肉が起こり、
薄い部分が破れたり、収縮むらが発生する等のトラブル
が発生する。石油樹脂配合量は2質量%以上ならば一応
安定製膜可能であるが、偏肉をさらに少なくしようと考
えるならば10質量%以上配合が好ましい。また、石油
樹脂配合量が30質量%を越える場合は吐出変動が発生
し、原反(延伸前のシート)の偏肉が起こり、延伸が困
難になる。石油樹脂の配合量は30質量%以下である
が、延伸性を考慮するならば20質量%以下が好まし
い。The content of petroleum resin in the core layer is 2 to 30% by mass, preferably 10 to 20% by mass. If the content of the petroleum resin is less than 2% by mass, the stretching point may fluctuate, the film formation may not be stable, and uneven thickness of the film may occur.
Problems such as breakage of thin parts and uneven shrinkage occur. If the amount of the petroleum resin compounded is 2% by mass or more, stable film formation is possible, but if it is intended to further reduce the uneven thickness, it is preferably 10% by mass or more. Further, when the content of the petroleum resin is more than 30% by mass, discharge variation occurs, uneven thickness of the raw fabric (sheet before stretching) occurs, and stretching becomes difficult. The blending amount of the petroleum resin is 30% by mass or less, but 20% by mass or less is preferable in consideration of stretchability.
【0013】本発明の熱収縮フィルムの芯層には、密度
が0.870g/cm3〜0.935g/cm3のポリエ
チレン系樹脂が用いられる。ポリエチレン系樹脂の密度
が下限に満たないと原反成形不良となり、上限を超える
と延伸は可能であるが熱収縮率不足となる。ポリエチレ
ン系樹脂は1種類でも良いし、密度の異なった複数の樹
脂でも良いが、各樹脂の密度はそれぞれ0.870g/
cm3〜0.935g/cm3の範囲にあることが必要で
ある。[0013] core layer of a heat shrinkable film of the present invention has a density polyethylene resin 0.870g / cm 3 ~0.935g / cm 3 is used. If the density of the polyethylene-based resin is less than the lower limit, raw material forming failure occurs, and if it exceeds the upper limit, stretching is possible but the heat shrinkage rate becomes insufficient. The polyethylene resin may be one kind or a plurality of resins having different densities, but the density of each resin is 0.870 g /
It must be in the range of cm 3 to 0.935 g / cm 3 .
【0014】中でも芯層のポリエチレン系樹脂は、密度
0.920〜0.935g/cm3のポリエチレン系樹
脂と、密度0.870〜0.915g/cm3のポリエ
チレン系樹脂の混合物である場合が収縮温度範囲を広げ
る点で好ましい。更に密度0.920〜0.935g/
cm3のポリエチレン系樹脂の割合が芯層のポリエチレ
ン系樹脂中の5〜20質量%、密度0.870〜0.9
15g/cm3のポリエチレン系樹脂の割合が芯層のポ
リエチレン系樹脂中の95〜80質量%の場合が安定製
膜のために特に好ましい。Among them, the polyethylene resin of the core layer may be a mixture of a polyethylene resin having a density of 0.920 to 0.935 g / cm 3 and a polyethylene resin having a density of 0.870 to 0.915 g / cm 3. It is preferable in that the shrinkage temperature range is widened. Furthermore, the density is 0.920 to 0.935 g /
The proportion of the polyethylene resin of cm 3 is 5 to 20% by mass in the polyethylene resin of the core layer, and the density is 0.870 to 0.9.
It is particularly preferable for the stable film formation that the proportion of the polyethylene resin of 15 g / cm 3 is 95 to 80% by mass in the polyethylene resin of the core layer.
【0015】芯層中のポリエチレン系樹脂の割合は、7
0〜98質量%、好ましくは80〜90質量%である。
ポリエチレン系樹脂の割合が下限に満たないと吐出変動
が発生し、延伸が困難になる。上限を超えると延伸点が
変動し、フィルムの偏肉が起こる。The proportion of polyethylene resin in the core layer is 7
It is 0 to 98% by mass, preferably 80 to 90% by mass.
If the proportion of the polyethylene-based resin is less than the lower limit, discharge fluctuations occur and stretching becomes difficult. If the upper limit is exceeded, the stretching point will fluctuate, causing uneven thickness of the film.
【0016】芯層のポリエチレン系樹脂としては、高圧
法の低密度ポリエチレン(密度0.910〜0.935
g/cm3)、直鎖状低密度ポリエチレン(密度0.9
10〜0.935g/cm3)、直鎖状超低密度ポリエ
チレン(密度0.870〜0.910g/cm3)、メ
タロセン系触媒を用いた低密度ポリエチレン(密度0.
910〜0.935g/cm3)、メタロセン系触媒を
用いた超低密度ポリエチレン(密度0.870〜0.9
10g/cm3)が用いられる。上記したポリエチレン
系樹脂には、本発明の目的とする物性を損なわない範囲
で、他のモノマーと共重合された共重合樹脂も含まれ
る。コモノマーの量はその種類ほかの条件にもよるが、
モノマー全質量の20質量%程度まで使用することが出
来る。コモノマーの種類としては、ブテン-1、ヘキセン
-1、オクテン-1、4メチルペンテン-1等が用いられる。As the polyethylene resin for the core layer, low density polyethylene (density 0.910 to 0.935) prepared by the high pressure method is used.
g / cm 3 ), linear low-density polyethylene (density 0.9
10 to 0.935 g / cm 3 ), linear ultra low density polyethylene (density 0.870 to 0.910 g / cm 3 ), low density polyethylene using a metallocene catalyst (density 0.
910 to 0.935 g / cm 3 ), ultra low density polyethylene using metallocene catalyst (density 0.870 to 0.9
10 g / cm 3 ) is used. The above-mentioned polyethylene-based resin also includes a copolymer resin copolymerized with another monomer as long as the physical properties aimed at by the present invention are not impaired. The amount of comonomer depends on the type and other conditions,
It is possible to use up to about 20% by mass of the total mass of the monomers. Types of comonomers include butene-1, hexene
-1, octene-1, 4-methylpentene-1 and the like are used.
【0017】本発明の熱収縮フィルムの表面層は、密度
0.905g/cm3以上、好ましくは0.910〜
0.930g/cm3のポリエチレン系樹脂からなる。
ポリエチレン系樹脂の密度が下限に満たないと、チュー
ブラー法では延伸時のバブル内面でのブロッキング、外
面と触れ止めリングとの滑り不良による延伸不安定が発
生する。テンター法ではロールへのべとつき及びチャッ
キング外れが発生する。ポリエチレン系樹脂の密度が高
すぎる場合は特に問題は発生しないが、熱収縮率が低く
なり、低温収縮フィルムとしては不満足なものとなる。
なお、2つの表面層の樹脂構成は、同一でも良いし、異
なっても良い。The surface layer of the heat shrinkable film of the present invention has a density of 0.905 g / cm 3 or more, preferably 0.910.
It is made of polyethylene resin of 0.930 g / cm 3 .
If the density of the polyethylene-based resin is less than the lower limit, the tubular method may cause blocking on the inner surface of the bubble during stretching and unstable drawing due to poor slip between the outer surface and the touch-preventing ring. In the tenter method, stickiness to the roll and unchucking occur. If the density of the polyethylene-based resin is too high, no particular problem will occur, but the heat shrinkage rate will be low and the low temperature shrinkable film will be unsatisfactory.
The resin configurations of the two surface layers may be the same or different.
【0018】本発明の熱収縮フィルムの表面層に使用さ
れる密度0.905g/cm3以上のポリエチレン系樹
脂としては、高圧法の低密度ポリエチレン(密度0.9
10〜0.940g/cm3)、高密度ポリエチレン
(密度0.940〜0.960g/cm3)、直鎖状低
密度ポリエチレン(密度0.910〜0.940g/c
m3)、直鎖状超低密度ポリエチレン(密度0.905
〜0.910g/cm3)、メタロセン系触媒を用いた
低密度ポリエチレン(密度0.910〜0.940g/
cm3)、メタロセン系触媒を用いた超低密度ポリエチ
レン(密度0.905〜0.910g/cm3)が用い
られる。上記したポリエチレン系樹脂には、本発明の目
的とする物性を損なわない範囲で、他のモノマーと共重
合された共重合樹脂も含まれる。コモノマーの量はその
種類ほかの条件にもよるが、モノマー全重量の20質量
%程度まで使用することが出来る。コモノマーの種類と
しては、ブテン−1、ヘキセン−1、オクテン−1、4
メチルペンテン−1等が用いられる。The polyethylene resin having a density of 0.905 g / cm 3 or more used for the surface layer of the heat-shrinkable film of the present invention includes low density polyethylene (density 0.9
10 to 0.940 g / cm 3 ), high density polyethylene (density 0.940 to 0.960 g / cm 3 ), linear low density polyethylene (density 0.910 to 0.940 g / c)
m 3 ), linear ultra-low density polyethylene (density 0.905
˜0.910 g / cm 3 ), low density polyethylene using a metallocene catalyst (density 0.910 to 0.940 g /
cm 3 ), and ultra-low density polyethylene (density 0.905 to 0.910 g / cm 3 ) using a metallocene catalyst. The above-mentioned polyethylene-based resin also includes a copolymer resin copolymerized with another monomer as long as the physical properties aimed at by the present invention are not impaired. Although the amount of the comonomer depends on the type and other conditions, it can be used up to about 20% by mass of the total weight of the monomers. The types of comonomer include butene-1, hexene-1, octene-1, 4
Methylpentene-1 or the like is used.
【0019】表面層と芯層の層比については特に定めな
いが、表面層/芯層/表面層の3層構成のフィルムの場
合、各層の厚さの比が2:1:2〜1:10:1の範囲
にあると、良好な偏肉のないシートが得られる。The layer ratio of the surface layer to the core layer is not particularly specified, but in the case of a film having a three-layer structure of surface layer / core layer / surface layer, the thickness ratio of each layer is 2: 1: 2-1 :. Within the range of 10: 1, a good sheet without uneven thickness can be obtained.
【0020】芯層あるいは表面層の樹脂には、必要な特
性を付与するために、プラスチック加工で通常用いられ
る添加剤すなわち滑剤、帯電防止剤、ブロッキング防止
剤、酸化防止剤等を用いても良い。To the resin for the core layer or the surface layer, in order to impart necessary properties, additives usually used in plastics processing, that is, lubricants, antistatic agents, antiblocking agents, antioxidants and the like may be used. .
【0021】本発明の熱収縮フィルムを製造するには、
密度0.905g/cm3以上のポリエチレン系樹脂か
らなる2つの表面層と、石油樹脂2〜30質量%、密度
0.870〜0.935g/cm3のポリエチレン系樹
脂98〜70質量%の混合樹脂からなる芯層を共押出し
し、10〜100kGyの電子線を照射した後、縦及び
横方向に3〜10倍に延伸する。製造方法としてはチュ
ーブラー法、テンター法のどちらでも良いが、熱収縮率
の縦横バランスの面からチューブラー法が好ましい。To produce the heat-shrinkable film of the present invention,
A mixture of two surface layers made of polyethylene resin having a density of 0.905 g / cm 3 or more, and 2 to 30 mass% of petroleum resin and 98 to 70 mass% of polyethylene resin having a density of 0.870 to 0.935 g / cm 3. A resin core layer is coextruded, irradiated with an electron beam of 10 to 100 kGy, and then stretched 3 to 10 times in the machine and transverse directions. As a manufacturing method, either a tubular method or a tenter method may be used, but the tubular method is preferable from the viewpoint of longitudinal and lateral balance of heat shrinkage.
【0022】本発明の熱収縮フィルムは、延伸前に電子
線照射する必要がある。電子線を照射しないでも延伸は
可能であるが、延伸が非常に不安定で厚みムラの多いフ
ィルムとなるばかりでなく、出来上がったフィルムは耐
熱性がなく、包装時、穴の開きやすいフィルムとなる。
電子線照射線量は10〜100kGyが必要であり、好
ましくは30〜70kGyである。電子線照射線量が1
0kGyに満たないと、延伸が不安定で厚薄の大きいフ
ィルムとなる。100kGyを超えると延伸は安定し、
厚みムラも少なく、加熱収縮率も必要な値が得られる
が、包装時の溶断シールカット性が不良で、使用に耐え
られるフィルムとはならない。電子線照射はチューブラ
ー法シートの場合には、シートをフラットなテープ状と
してシートの両面から、テンター法シートの場合には、
シートの片面から照射することが好ましい。The heat-shrinkable film of the present invention needs to be irradiated with an electron beam before stretching. Stretching is possible without irradiating the electron beam, but not only does the film become very unstable and has a large thickness variation, the finished film does not have heat resistance and becomes a film that easily punctures during packaging. .
The electron beam irradiation dose is required to be 10 to 100 kGy, preferably 30 to 70 kGy. Electron beam irradiation dose is 1
If it is less than 0 kGy, stretching is unstable and a thick and thick film is obtained. If it exceeds 100 kGy, stretching is stable,
Although the thickness unevenness is small and the required heat shrinkage ratio is obtained, the film does not have the durability to use because of its poor melt-cut seal cut property during packaging. For electron beam irradiation, in the case of a tubular method sheet, the sheet is made into a flat tape shape from both sides of the sheet, and in the case of a tenter method sheet,
It is preferable to irradiate from one side of the sheet.
【0023】こうして出来た本発明の熱収縮フィルムは
低温での熱収縮率に優れ、100℃の加熱収縮率が縦横
共35%以上、90℃の加熱収縮率が縦横共20%以上
の熱収縮率を有する超低温収縮フィルムとなる。加熱収
縮率がこれらの価を満足する場合には、DVD包装時に
辺及び角にシワが全く残らない、優れた製品を得ること
が出来る。このような超低温収縮フィルムを得るために
は、上記した条件に加え、石油樹脂を除くポリエチレン
系樹脂(表面層と芯層の合計)の平均密度を0.910
g/cm3以下にするなどの手段が有効である。The heat-shrinkable film of the present invention thus produced has an excellent heat-shrinkage ratio at low temperatures, and has a heat-shrinkage ratio of 100 ° C. of 35% or more in both length and width and a heat shrinkage ratio of 90 ° C. of 20% or more in both length and width. It becomes an ultra-low temperature shrinkable film having a rate. When the heat shrinkage rate satisfies these values, it is possible to obtain an excellent product in which no wrinkles are left on the sides and corners during DVD packaging. In order to obtain such an ultra-low temperature shrinkable film, in addition to the above-mentioned conditions, the average density of polyethylene-based resins (total of surface layer and core layer) excluding petroleum resin is 0.910.
It is effective to use g / cm 3 or less.
【0024】[0024]
【実施例】以下に、本発明を実施例によって具体的に説
明するが、本発明はこれらの実施例によって限定される
ものではない。EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.
【0025】<平均密度の計算方法>なお、実施例、比
較例の平均密度の計算方法は下記のとおりである。例え
ばLLDPE1(密度0.915g/cm3)が20質
量部、LLDPE2(密度0.905g/cm3)が5
0質量部、LLDPE3(密度0.885g/cm3)
が30質量部の場合以下の様に計算する。
平均密度=0.915×0.2+0.905×0.5+
0.885×0.3=0.901<Calculation Method of Average Density> The calculation method of average density in Examples and Comparative Examples is as follows. For example, 20 parts by mass of LLDPE1 (density 0.915 g / cm 3 ) and 5 parts of LLDPE2 (density 0.905 g / cm 3 ).
0 parts by mass, LLDPE3 (density 0.885 g / cm 3 )
When is 30 parts by mass, it is calculated as follows. Average density = 0.915 × 0.2 + 0.905 × 0.5 +
0.885 x 0.3 = 0.901
【0026】実施例1
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)70質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)10質量部、石油樹脂(荒
川化学社製アルコンP−125)10質量部を混練り
し、表面層に密度0.912g/cm3のポリエチレン
系樹脂(ダウケミカル社製アテイン4201)を使用
し、環状ダイスにて押出し、急冷することにより、厚さ
450μmのチューブを得た。このチューブを折り畳
み、表裏から電子線照射装置を用いて50kGyの電子
線を照射した。このチューブを定法により縦6倍、横5
倍に2軸延伸を行い、厚さ15μmの3層フィルムを得
た。このフィルムの100℃の加熱収縮率は40%であ
った。このフィルムを用い、DVDケースのシュリンク
包装を実施したところ評価点は4点で、美しい仕上がり
が得られた。Example 1 70 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co.) in the core layer, and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co.) 2042A) 10 parts by mass, 10 parts by mass of a polyethylene resin (DFDB1088 manufactured by Nippon Unicar Co., Ltd.) having a density of 0.885 g / cm 3 , and 10 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) are kneaded to form a surface layer. A polyethylene resin having a density of 0.912 g / cm 3 (Atein 4201 manufactured by Dow Chemical Co., Ltd.) was used for extrusion with a ring die, followed by rapid cooling to obtain a tube having a thickness of 450 μm. This tube was folded, and an electron beam of 50 kGy was irradiated from the front and back using an electron beam irradiation device. This tube is 6 times in length and 5 in width by the standard method.
Biaxial stretching was performed twice to obtain a three-layer film having a thickness of 15 μm. The heat shrinkage percentage of this film at 100 ° C. was 40%. When a shrink wrap of a DVD case was carried out using this film, the evaluation point was 4, and a beautiful finish was obtained.
【0027】実施例2
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)45質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)15質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)30質量部、石油樹脂(荒
川化学社製アルコンP−125)10質量部を混練り
し、表面層に密度0.912g/cm3のポリエチレン
系樹脂(ダウケミカル社製アテイン4201)を使用
し、環状ダイスにて押出し、急冷することにより、厚さ
450μmのチューブを得た。このチューブを折り畳
み、表裏から電子線照射装置を用いて50kGyの電子
線を照射した。このチューブを定法により縦6倍、横5
倍に2軸延伸を行い、厚さ15μmの3層フィルムを得
た。このフィルムの100℃の加熱収縮率は46%であ
った。このフィルムを用い、DVDケースのシュリンク
包装を実施したところ、評価点は4.5点であった。Example 2 45 parts by mass of a polyethylene-based resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co., Ltd.) and a polyethylene-based resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co., Ltd.) were used for the core layer. 2042A) 15 parts by mass, 30 parts by mass of a polyethylene resin (DFDB1088 manufactured by Nippon Unicar Co., Ltd.) having a density of 0.885 g / cm 3 , and 10 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) are kneaded to form a surface layer. A polyethylene resin having a density of 0.912 g / cm 3 (Atein 4201 manufactured by Dow Chemical Co., Ltd.) was used for extrusion with a ring die, followed by rapid cooling to obtain a tube having a thickness of 450 μm. This tube was folded, and an electron beam of 50 kGy was irradiated from the front and back using an electron beam irradiation device. This tube is 6 times in length and 5 in width by the standard method.
Biaxial stretching was performed twice to obtain a three-layer film having a thickness of 15 μm. The heat shrinkage percentage of this film at 100 ° C. was 46%. When a shrink wrap of a DVD case was carried out using this film, the evaluation point was 4.5 points.
【0028】実施例3
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)65質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、石油
樹脂(荒川化学社製アルコンP−125)25質量部を
混練りし、表面層に密度0.912g/cm3のポリエ
チレン系樹脂(ダウケミカル社製アテイン4201)を
使用し、環状ダイスにて押出し急冷することにより、厚
さ450μmのチューブを得た。このチューブを折り畳
み、表裏から電子線照射装置を用いて50kGyの電子
線を照射した。このチューブを定法により縦6倍、横5
倍に2軸延伸を行い、厚さ15μmの3層フィルムを得
た。延伸はやや不安定であった。このフィルムの100
℃の加熱収縮率は51%であった。このフィルムを用
い、DVDケースのシュリンク包装を実施したところ、
評価点は5点でシワもなく美しい仕上がりが得られた。Example 3 65 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co., Ltd.) and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co., Ltd.) were used for the core layer. 2042A) 10 parts by mass and petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) 25 parts by mass are kneaded, and a polyethylene resin having a density of 0.912 g / cm 3 (Atein 4201 manufactured by Dow Chemical Co., Ltd.) is used for the surface layer. Then, it was extruded with an annular die and rapidly cooled to obtain a tube having a thickness of 450 μm. This tube was folded, and an electron beam of 50 kGy was irradiated from the front and back using an electron beam irradiation device. This tube is 6 times in length and 5 in width by the standard method.
Biaxial stretching was performed twice to obtain a three-layer film having a thickness of 15 μm. The stretching was somewhat unstable. 100 of this film
The heat shrinkage rate at ° C was 51%. Using this film to shrink-wrap DVD cases,
The evaluation score was 5 and a beautiful finish was obtained without wrinkles.
【0029】比較例1
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)70質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)20質量部を混練りし、表
面層に密度0.912g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4201)を使用し、環状
ダイスにて押出し急冷することにより厚さ450μmの
チューブを得た。このチューブを折り畳み、表裏から電
子線照射装置を用いて50kGyの電子線を照射した。
このチューブを定法により縦6倍、横5倍に2軸延伸を
行ったが延伸点が安定せず、偏肉の悪い3層フィルムが
得られた。Comparative Example 1 70 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co., Ltd.) and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co., Ltd.) were used for the core layer. 2042A) 10 parts by weight, the polyethylene resin (manufactured by Nippon Unicar Company Limited DFDB1088 density 0.885 g / cm 3) 20 parts by weight were kneaded, polyethylene resin density of 0.912 g / cm 3 on the surface layer (Dow Chemical Company Atein 4201) was used, and a tube having a thickness of 450 μm was obtained by extrusion with an annular die and rapid cooling. This tube was folded, and an electron beam of 50 kGy was irradiated from the front and back using an electron beam irradiation device.
This tube was biaxially stretched 6 times in the longitudinal direction and 5 times in the lateral direction by a conventional method, but the stretching point was not stable, and a three-layer film with poor thickness deviation was obtained.
【0030】比較例2
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)45質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)10質量部、石油樹脂(荒
川化学社製アルコンP−125)35質量部を混練り
し、表面層に密度0.912g/cm3のポリエチレン
系樹脂(ダウケミカル社製アテイン4201)を使用
し、環状ダイスにて押出し急冷することにより、厚さ4
50μmのチューブを得た。このチューブを折り畳み、
表裏から電子線照射装置を用いて50kGyの電子線を
照射した。このチューブを定法により縦6倍、横5倍に
2軸延伸を行おうとしたが、延伸できなかった。Comparative Example 2 45 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co.) and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co., Ltd.) were used for the core layer. 2042A) 10 parts by mass, 10 parts by mass of a polyethylene resin (DFDB1088 manufactured by Nippon Unicar Co., Ltd.) having a density of 0.885 g / cm 3 , and 35 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) are kneaded to form a surface layer. A polyethylene resin (Atein 4201 manufactured by Dow Chemical Co., Ltd.) having a density of 0.912 g / cm 3 is used as the material and is extruded with a ring die to be rapidly cooled to obtain a thickness of 4
A 50 μm tube was obtained. Fold this tube,
An electron beam of 50 kGy was irradiated from the front and back using an electron beam irradiation device. This tube was biaxially stretched 6 times in the longitudinal direction and 5 times in the lateral direction by a conventional method, but could not be stretched.
【0031】比較例3
芯層に密度0.868g/cm3のポリエチレン系樹脂
(ダウケミカル社製エンゲージEG8150)90質量
部、石油樹脂(荒川化学社製アルコンP−125)10
質量部を混練りし、表面層に密度0.912g/cm3
のポリエチレン系樹脂(ダウケミカル社製アテイン42
01)を使用し、環状ダイスにて押出し、急冷したが原
反成形不良で製膜できなかった。Comparative Example 3 90 parts by mass of a polyethylene-based resin (Engage EG8150 manufactured by Dow Chemical Co., Ltd.) having a density of 0.868 g / cm 3 and 10 parts of petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) in the core layer.
Kneading parts by mass, the surface layer has a density of 0.912 g / cm 3
Polyethylene resin (Atein 42 manufactured by Dow Chemical Co., Ltd.
No. 01) was used and the mixture was extruded with a ring die and rapidly cooled.
【0032】比較例4
芯層に密度0.950g/cm3のポリエチレン系樹脂
(日本ポリオレフィン社製E807F)90質量部、石
油樹脂(荒川化学社製アルコンP−125)10質量部
を混練りし、表面層に密度0.912g/cm3のポリ
エチレン系樹脂(ダウケミカル社製アテイン4201)
を使用し、環状ダイスにて押出し、急冷することによ
り、厚さ450μmのチューブを得た。このチューブを
折り畳み、表裏から電子線照射装置を用いて50kGy
の電子線を照射した。このチューブを定法により縦6
倍、横5倍に2軸延伸を行い、厚さ15μmの3層フィ
ルムを得た。このフィルムの100℃の加熱収縮率は1
0%であった。このフィルムを用い、DVDケースのシ
ュリンク包装を実施したが評価点は1.5点で、仕上が
り不良だった。Comparative Example 4 90 parts by mass of a polyethylene resin (E807F manufactured by Nippon Polyolefin Co., Ltd.) having a density of 0.950 g / cm 3 and 10 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) were kneaded in the core layer. , Polyethylene resin with a density of 0.912 g / cm 3 on the surface layer (Atein 4201 manufactured by Dow Chemical Co.)
Was extruded with an annular die and rapidly cooled to obtain a tube having a thickness of 450 μm. Fold this tube and use the electron beam irradiation device from the front and back to 50 kGy
Was irradiated with an electron beam. This tube is vertically 6 by standard method.
The film was biaxially stretched twice and five times horizontally to obtain a three-layer film having a thickness of 15 μm. The heat shrinkage rate of this film at 100 ° C is 1
It was 0%. Shrink wrapping of a DVD case was carried out using this film, but the evaluation point was 1.5 and the finish was poor.
【0033】比較例5
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)70質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)10質量部、石油樹脂(荒
川化学社製アルコンP−125)10質量部を混練り
し、表面層に密度0.895g/cm3のポリエチレン
系樹脂(ダウケミカル社製アフィニティPF1140)
を使用し、環状ダイスにて押出し、急冷することによ
り、厚さ450μmのチューブを得た。このチューブを
折り畳み、表裏から電子線照射装置を用いて50kGy
の電子線を照射した。このチューブを定法により縦6
倍、横5倍に2軸延伸を行ったが触れ止めリングとの滑
りが悪く安定延伸ができなかった。Comparative Example 5 70 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co., Ltd.) and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co., Ltd.) were used for the core layer. 2042A) 10 parts by mass, 10 parts by mass of a polyethylene resin (DFDB1088 manufactured by Nippon Unicar Co., Ltd.) having a density of 0.885 g / cm 3 , and 10 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) are kneaded to form a surface layer. Polyethylene resin with a density of 0.895 g / cm 3 (Affinity PF1140 manufactured by Dow Chemical Co.)
Was extruded with an annular die and rapidly cooled to obtain a tube having a thickness of 450 μm. Fold this tube and use the electron beam irradiation device from the front and back to 50 kGy
Was irradiated with an electron beam. This tube is vertically 6 by standard method.
The film was biaxially stretched twice and five times horizontally, but slippage with the touch stop ring was poor and stable stretching could not be performed.
【0034】比較例6
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)70質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)10質量部、石油樹脂(荒
川化学社製アルコンP−125)10質量部を混練り
し、表面層に密度0.912g/cm3のポリエチレン
系樹脂(ダウケミカル社製アテイン4201)を使用
し、環状ダイスにて押出し、急冷することにより、厚さ
450μmのチューブを得た。このチューブを折り畳
み、表裏から電子線照射装置を用いて5kGyの電子線
を照射した。このチューブを定法により縦6倍、横5倍
に2軸延伸を行ったが延伸点が不安定で安定延伸ができ
なかった。Comparative Example 6 70 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co.) and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co., Ltd.) were used for the core layer. 2042A) 10 parts by mass, 10 parts by mass of a polyethylene resin (DFDB1088 manufactured by Nippon Unicar Co., Ltd.) having a density of 0.885 g / cm 3 , and 10 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) are kneaded to form a surface layer. A polyethylene resin having a density of 0.912 g / cm 3 (Atein 4201 manufactured by Dow Chemical Co., Ltd.) was used for extrusion with a ring die, followed by rapid cooling to obtain a tube having a thickness of 450 μm. This tube was folded and irradiated with an electron beam of 5 kGy from the front and back using an electron beam irradiation device. This tube was biaxially stretched 6 times in the longitudinal direction and 5 times in the lateral direction by a conventional method, but the stretching point was unstable and stable stretching could not be performed.
【0035】比較例7
芯層に密度0.905g/cm3のポリエチレン系樹脂
(ダウケミカル社製アテイン4203)70質量部、密
度0.930g/cm3のポリエチレン系樹脂(ダウケ
ミカル社製ダウレックス2042A)10質量部、密度
0.885g/cm3のポリエチレン系樹脂(日本ユニ
カー社製DFDB1088)10質量部、石油樹脂(荒
川化学社製アルコンP−125)10質量部を混練り
し、表面層に密度0.912g/cm3のポリエチレン
系樹脂(ダウケミカル社製アテイン4201)を使用
し、環状ダイスにて押出し、急冷することにより、厚さ
450μmのチューブを得た。このチューブを折り畳
み、表裏から電子線照射装置を用いて120kGyの電
子線を照射した。このチューブを定法により縦6倍、横
5倍に2軸延伸を行い、厚さ15μmの3層フィルムを
得た。このフィルムの100℃の加熱収縮率は40%で
あった。このフィルムを用い、DVDケースのシュリン
ク包装を実施したが溶断シールのカット性が不良で安定
した包装ができなかった。Comparative Example 7 70 parts by mass of a polyethylene resin having a density of 0.905 g / cm 3 (Atein 4203 manufactured by Dow Chemical Co.) in the core layer, and a polyethylene resin having a density of 0.930 g / cm 3 (Dow Rex manufactured by Dow Chemical Co.) 2042A) 10 parts by mass, 10 parts by mass of a polyethylene resin (DFDB1088 manufactured by Nippon Unicar Co., Ltd.) having a density of 0.885 g / cm 3 , and 10 parts by mass of a petroleum resin (Arcon P-125 manufactured by Arakawa Chemical Co., Ltd.) are kneaded to form a surface layer. A polyethylene resin having a density of 0.912 g / cm 3 (Atein 4201 manufactured by Dow Chemical Co., Ltd.) was used for extrusion with a ring die, followed by rapid cooling to obtain a tube having a thickness of 450 μm. This tube was folded, and 120 kGy of electron beam was irradiated from the front and back using an electron beam irradiation device. This tube was biaxially stretched 6 times in length and 5 times in width by a conventional method to obtain a three-layer film having a thickness of 15 μm. The heat shrinkage percentage of this film at 100 ° C. was 40%. Shrink wrapping of a DVD case was carried out using this film, but the cutability of the fusing seal was poor, and stable wrapping was not possible.
【0036】こうして得たフィルムの90℃と100℃
の熱収縮性、包装仕上がり、フィルムの延伸性について
測定し、下記の基準で評価した。結果を表1及び表2に
示す。
<フィルムの90℃と100℃の熱収縮性>100mm
×100mmの寸法にフィルムの中央部と両端部から切
り出す。このフィルムを金網製の蓋付きカゴに入れ、1
00℃のグリセリンバスに30秒浸漬する。カゴごと冷
却水に漬け、次式により熱収縮率を求める。
加熱収縮率(%)=〔(浸漬前の寸法−浸漬後の寸法)
/(浸漬前の寸法)〕×10090 ° C. and 100 ° C. of the film thus obtained
The heat shrinkability, the packaging finish, and the stretchability of the film were measured and evaluated according to the following criteria. The results are shown in Tables 1 and 2. <Heat shrinkage of film at 90 ° C and 100 ° C> 100 mm
Cut out from the center and both ends of the film to a dimension of × 100 mm. Put this film in a basket made of wire mesh and 1
Immerse in a glycerin bath at 00 ° C. for 30 seconds. The basket is immersed in cooling water, and the heat shrinkage is calculated by the following formula. Heat shrinkage (%) = [(dimension before immersion-dimension after immersion)
/ (Dimension before immersion)] × 100
【0037】なお、一般のポリプロピレン熱収縮フィル
ムは100℃で10〜15%、ポリエチレン系の架橋熱
収縮フィルムでは20〜30%、ポリ塩化ビニル系熱収
縮フィルムでは40%前後である。90℃のフィルムの
熱収縮性は上記グリセリンバスの温度を90℃とする以
外は100℃の場合と同様にして測定した。なお、一般
のポリプロピレン熱収縮フィルムは90℃で5〜7%、
ポリエチレン系の架橋熱収縮フィルムでは10〜15
%、ポリ塩化ビニル系熱収縮フィルムでは35%前後で
ある。It should be noted that general polypropylene heat-shrinkable films are 10 to 15% at 100 ° C., polyethylene crosslinked heat-shrinkable films are 20 to 30%, and polyvinyl chloride heat-shrinkable films are around 40%. The heat shrinkability of the film at 90 ° C. was measured in the same manner as at 100 ° C. except that the temperature of the glycerin bath was 90 ° C. In addition, the general polypropylene heat shrink film is 5 to 7% at 90 ° C,
10 to 15 for polyethylene-based crosslinked heat shrink film
%, About 35% for a polyvinyl chloride-based heat-shrinkable film.
【0038】<包装仕上がり評価法>市販のDVDケー
スを6個の空気抜け穴を開けたフィルムで包み、3方を
熱刃でシールカットし、ケーユーシステム製のシュリン
クトンネルに140℃、5秒間通した。収縮後のタイト
性、角や辺のシワの有無から5段階で包装仕上がりを評
価し、6回の平均値を示した。
5:角、辺にシワが無くタイト性が良好
4:角、辺にシワが1カ所あるがタイト性は良好
3:角、辺にシワが2カ所あるがタイト性は良好
2:角、辺にシワが4カ所共あるがタイト性は良好
1:タイト性不良<Evaluation Method of Packaging Finish> A commercially available DVD case is wrapped with a film having six air vent holes, three sides are seal-cut with a hot blade, and the resultant is passed through a shrink tunnel manufactured by KE system at 140 ° C. for 5 seconds. . The packaging finish was evaluated on a scale of 5 from the tightness after shrinkage and the presence or absence of wrinkles on the corners and sides, and the average value of 6 times was shown. 5: No wrinkles on corners and sides, good tightness 4: Good wrinkle on corners, 1 side, but good tightness 3: Corner, 2 wrinkles on sides, good tightness 2: Corners, sides There are four wrinkles on the surface, but the tightness is good 1: The tightness is poor
【0039】<フィルムの延伸性>延伸性は延伸開始後
破断までの時間で評価した。
◎:10時間以上延伸可
○:3時間以上10時間未満延伸可
△:30分以上〜3時間未満で破断
×:30分未満で破断<Stretchability of Film> Stretchability was evaluated by the time from the start of stretching to the break. ◎: Stretching is possible for 10 hours or more ○: Stretching is possible for 3 hours or more and less than 10 hours Δ: Breaking for 30 minutes or more and less than 3 hours x: Breaking for less than 30 minutes
【0040】[0040]
【表1】 [Table 1]
【0041】[0041]
【表2】 [Table 2]
【0042】各表中、「部」は質量部を表す。表から本
発明の熱収縮フィルムは、90℃及び100℃という比
較的低温での熱収縮率が塩化ビニル系熱収縮フィルムに
匹敵し、角、辺にシワのないタイトな包装ができること
が明らかである。In each table, "part" means part by mass. From the table, it is clear that the heat-shrinkable film of the present invention has a heat shrinkage ratio at a relatively low temperature of 90 ° C. and 100 ° C. comparable to that of a vinyl chloride-based heat-shrinkable film, and can be tightly packed without wrinkles on the corners and sides. is there.
【0043】[0043]
【発明の効果】以上の結果から明らかなように、本発明
の方法によって得られる熱収縮フィルムは、DVDやビ
デオ等の扁平な被包装物を包装するに好適な熱収縮フィ
ルムであり、特に低温収縮性に優れ、角や辺にシワの入
らない、包装仕上がりの良いポリエチレン系超低温熱収
縮フィルムである。また、透明性に優れ、腰が強く、包
装時の作業性が良い熱収縮フィルムである。さらにま
た、溶断シールカット性の良いフィルムである。As is clear from the above results, the heat-shrinkable film obtained by the method of the present invention is a heat-shrinkable film suitable for packaging flat objects to be packaged such as DVDs and videos, especially at low temperatures. A polyethylene ultra-low temperature heat-shrinkable film with excellent shrinkability, with no wrinkles on the corners and sides and good packaging finish. Further, it is a heat-shrinkable film which is excellent in transparency, has a strong elasticity, and has good workability during packaging. Furthermore, it is a film with good fusing and seal-cutting properties.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) //(C08L 23/04 C08L 57:02 57:02) B29K 23:00 B29K 23:00 105:02 105:02 B29L 7:00 B29L 7:00 9:00 9:00 Fターム(参考) 4F071 AA15 AA39 AA82 AF54 AF61 AH04 BB06 BB08 BB09 BC01 BC12 4F073 AA10 AA32 BA06 BA07 BB01 CA42 HA11 4F100 AK02B AK02H AK04A AK04B AK04C AL05B BA03 BA06 BA10B BA10C BA16 EH202 EJ383 EJ532 GB15 GB41 JA03 JA13A JA13B JA13C YY00 YY00A YY00B YY00C YY00H 4F210 AA04 AA49 AE01 AG01 AG03 AH54 AR12 RA05 RC02 RG02 RG07 RG09 RG24 RG43 RG67 4J002 BA012 BB031 GG02 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) // (C08L 23/04 C08L 57:02 57:02) B29K 23:00 B29K 23:00 105: 02 105 : 02 B29L 7:00 B29L 7:00 9:00 9:00 9:00 F term (reference) 4F071 AA15 AA39 AA82 AF54 AF61 AH04 BB06 BB08 BB09 BC01 BC12 4F073 AA10 AA32 BA06 BA07 BB01 CA42 HA11 4F100 AK02B AK02H BAK04A06 AL04 BA10B BA10C BA16 EH202 EJ383 EJ532 GB15 GB41 JA03 JA13A JA13B JA13C YY00 YY00A YY00B YY00C YY00H 4F210 AA04 AA49 AE01 AG01 AG03 AH54 AR12 RA05 RC02 RG02 RG02 BB02 RG02 BB01 RG67 4J02B02
Claims (4)
のポリエチレン系樹脂からなる2つの表面層と、石油樹
脂2〜30質量%、密度0.870〜0.935g/c
m3のポリエチレン系樹脂98〜70質量%の混合樹脂
からなる芯層を共押出しし、10〜100kGyの電子
線を照射した後、縦及び横方向に3〜10倍に延伸する
ことを特徴とするポリエチレン系2軸延伸熱収縮フィル
ムの製造方法。1. A density of 0.905 to 0.960 g / cm 3.
Two surface layers made of polyethylene resin, petroleum resin 2 to 30% by mass, density 0.870 to 0.935 g / c
A core layer made of a mixed resin of 98 to 70% by mass of m 3 polyethylene resin is coextruded, irradiated with an electron beam of 10 to 100 kGy, and then stretched 3 to 10 times in the longitudinal and transverse directions. A method for producing a polyethylene-based biaxially stretched heat-shrinkable film.
920〜0.935g/cm3のポリエチレン系樹脂
と、密度0.870〜0.915g/cm3のポリエチ
レン系樹脂の混合物である請求項1に記載のポリエチレ
ン系2軸延伸熱収縮フィルムの製造方法。2. The polyethylene resin of the core layer has a density of 0.
The method for producing a polyethylene biaxially stretched heat-shrinkable film according to claim 1, which is a mixture of a polyethylene resin having a density of 920 to 0.935 g / cm 3 and a polyethylene resin having a density of 0.870 to 0.915 g / cm 3. .
ポリエチレン系2軸延伸熱収縮フィルム。3. A polyethylene-based biaxially stretched heat-shrinkable film produced by the method according to claim 1.
上、90℃の加熱収縮率が縦横共20%以上である請求
項3に記載のポリエチレン系2軸延伸熱収縮フィルム。4. The polyethylene-based biaxially stretched heat-shrinkable film according to claim 3, wherein the heat shrinkage at 100 ° C. is 35% or more in both length and width and the heat shrinkage rate at 90 ° C. is 20% or more in both length and width.
Priority Applications (1)
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JP2001344137A JP2003145695A (en) | 2001-11-09 | 2001-11-09 | Method for manufacturing polyethylenic heat-shrinkable film |
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JP2001344137A JP2003145695A (en) | 2001-11-09 | 2001-11-09 | Method for manufacturing polyethylenic heat-shrinkable film |
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JPWO2010107052A1 (en) * | 2009-03-17 | 2012-09-20 | 株式会社プライムポリマー | Polypropylene for film capacitor, polypropylene sheet for film capacitor, production method thereof, and use thereof |
JP2012212672A (en) * | 2011-03-23 | 2012-11-01 | Asahi Kasei Chemicals Corp | Polyethylene-based resin composition for crosslinked insulator and high-frequency coaxial cable using the same |
JP2012229443A (en) * | 2004-11-25 | 2012-11-22 | Mitsui Chemicals Inc | Propylene-based resin composition and use thereof |
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2001
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US9969853B2 (en) | 2004-11-25 | 2018-05-15 | Mitsui Chemicals, Inc. | Propylene based resin composition and use thereof |
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JP2012229443A (en) * | 2004-11-25 | 2012-11-22 | Mitsui Chemicals Inc | Propylene-based resin composition and use thereof |
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JP2014223808A (en) * | 2008-12-22 | 2014-12-04 | 興人フィルム&ケミカルズ株式会社 | Polyethylenic crosslinked shrinkable film |
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