JPH10119211A - Heat-shrinkable film - Google Patents
Heat-shrinkable filmInfo
- Publication number
- JPH10119211A JPH10119211A JP8274390A JP27439096A JPH10119211A JP H10119211 A JPH10119211 A JP H10119211A JP 8274390 A JP8274390 A JP 8274390A JP 27439096 A JP27439096 A JP 27439096A JP H10119211 A JPH10119211 A JP H10119211A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- film
- shrinkable
- layer
- molecular weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920006257 Heat-shrinkable film Polymers 0.000 title claims abstract description 26
- 229920000098 polyolefin Polymers 0.000 claims abstract description 23
- 229920001577 copolymer Polymers 0.000 claims description 12
- 239000000155 melt Substances 0.000 claims description 5
- 229920000642 polymer Polymers 0.000 claims description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 2
- -1 polyethylene Polymers 0.000 abstract description 11
- 238000007789 sealing Methods 0.000 abstract description 7
- 239000004698 Polyethylene Substances 0.000 abstract description 6
- 229920000573 polyethylene Polymers 0.000 abstract description 6
- 230000035939 shock Effects 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 55
- 238000004806 packaging method and process Methods 0.000 description 22
- 238000012360 testing method Methods 0.000 description 18
- 229920005989 resin Polymers 0.000 description 14
- 239000011347 resin Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 13
- 238000002844 melting Methods 0.000 description 7
- 230000008018 melting Effects 0.000 description 7
- 238000009826 distribution Methods 0.000 description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 5
- 239000005977 Ethylene Substances 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 239000002131 composite material Substances 0.000 description 5
- 229920000092 linear low density polyethylene Polymers 0.000 description 5
- 239000004707 linear low-density polyethylene Substances 0.000 description 5
- KWKAKUADMBZCLK-UHFFFAOYSA-N methyl heptene Natural products CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 230000002087 whitening effect Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000903 blocking effect Effects 0.000 description 3
- 210000005069 ears Anatomy 0.000 description 3
- 229920001903 high density polyethylene Polymers 0.000 description 3
- 239000004700 high-density polyethylene Substances 0.000 description 3
- 229920001684 low density polyethylene Polymers 0.000 description 3
- 239000004702 low-density polyethylene Substances 0.000 description 3
- 239000012968 metallocene catalyst Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 3
- 229920005673 polypropylene based resin Polymers 0.000 description 3
- 239000004800 polyvinyl chloride Substances 0.000 description 3
- 229920000915 polyvinyl chloride Polymers 0.000 description 3
- 229920003002 synthetic resin Polymers 0.000 description 3
- 239000000057 synthetic resin Substances 0.000 description 3
- 239000004711 α-olefin Substances 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 2
- WWUVJRULCWHUSA-UHFFFAOYSA-N 2-methyl-1-pentene Chemical compound CCCC(C)=C WWUVJRULCWHUSA-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- 229920005672 polyolefin resin Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- 229920010126 Linear Low Density Polyethylene (LLDPE) Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006225 ethylene-methyl acrylate Polymers 0.000 description 1
- 229920005680 ethylene-methyl methacrylate copolymer Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000011990 phillips catalyst Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Laminated Bodies (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Wrappers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、特定の性質を有す
る、長鎖分岐構造のポリオレフィンの層を有する熱収縮
性フィルムに関する。更に詳しくは、特定の溶融流動
性、分子量分布を兼ね備えた長鎖分岐構造のポリオレフ
ィンの層を有する、低熱収縮応力等の包装適性に優れた
熱収縮性フィルムに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat-shrinkable film having a polyolefin layer having a specific property and a long-chain branched structure. More specifically, the present invention relates to a heat-shrinkable film having a polyolefin layer having a long-chain branched structure having specific melt fluidity and molecular weight distribution and having excellent heat-shrinkage stress and other suitable packaging properties.
【0002】[0002]
【従来の技術】現在、包装技術の一分野として熱収縮性
フィルムを使用する熱収縮包装技術が存在し、多分野の
商品の包装に利用されている。ここにいう熱収縮包装と
は、被包装物全体を先ず熱収縮性フィルムで覆った後、
相対するフィルム間で溶断シールをして袋状の緩やかな
包装体とし、次に外部加熱をしてフィルムを収縮させ、
緊張包装状態にすることを言い、包装作業が簡単であ
り、一括包装適性を有し、外観に優れた包装状態が得ら
れる特徴を有する。2. Description of the Related Art At present, there is a heat shrink wrapping technique using a heat shrinkable film as one field of a wrapping technique, which is used for wrapping products in various fields. The heat shrink wrapping here means that the entire packaged object is first covered with a heat shrinkable film,
A fusing seal is made between the opposing films to form a bag-shaped loose package, and then the film is shrunk by external heating,
It refers to a tension-packed state, and is characterized in that the packaging operation is easy, the package is suitable for batch packaging, and a package with excellent appearance is obtained.
【0003】この熱収縮包装において熱収縮性フィルム
に要求される主要な条件としては、 フィルムの融点よりも低い加熱温度で熱収縮すること
(フィルムの溶融破れ、被包装体の過熱損傷を避ける等
のため)、熱収縮温度巾が広いこと(フィルムの熱的
特性自体に巾がある、熱収縮加工機械温度の調節が容易
である等のため)、フィルムの熱収縮応力は被包装体
の変形強度以下であること(フィルムの熱収縮応力が高
過ぎると、被包装体が変形して商品価値を落とす等のた
め)、フィルム溶断シール部の熱収縮後の機械特性が
高いこと(フィルムの溶断シール強度が低い場合は、熱
収縮包装後に引張応力が集中して破袋しやすいため)、
熱収縮包装後、フィルム溶断シール部に収縮不完全部
分を残さないこと(該収縮不完全部分を残すと、包装体
の外観が悪く、商品価値を落とす等のため)、熱収縮
後のフィルムが高透明性、高光沢性を有する他、フィル
ム溶断シール時に無臭性(商品価値、環境又は食品衛生
向上等のため)であること等が挙げられる。[0003] In this heat shrink wrapping, the main condition required for the heat shrinkable film is that the film shrinks at a heating temperature lower than the melting point of the film (for example, to avoid melting and tearing of the film and overheating damage of the packaged object, etc.). Wide heat shrink temperature range (because the thermal properties of the film itself are wide, easy to adjust the heat shrink processing machine temperature, etc.), the heat shrink stress of the film is the deformation of the package Strength or less (because if the heat shrinkage stress of the film is too high, the packaged body will be deformed and the commercial value will be reduced), and the mechanical properties of the film fusing seal after heat shrinkage are high (film fusing) If the sealing strength is low, the tensile stress will concentrate after heat shrink wrapping and the bag will break easily.)
After heat shrink wrapping, do not leave incompletely shrinkable parts in the film fusing seal part (leaving the incompletely shrinkable parts will result in poor appearance of the package and reduce the commercial value). In addition to high transparency and high gloss, the film is odorless at the time of film fusing sealing (for improving commercial value, environment or food hygiene, etc.).
【0004】従来、熱収縮性フィルムとしては、主とし
てポリエチレン、ポリプロピレン、ポリ塩化ビニール製
フィルムを二軸延伸処理して得られたフィルムが最も一
般的である。 二軸延伸ポリ塩化ビニルフィルムの場合
は、熱収縮後のフィルムの透明性、光沢性は優れている
ものの、通常の熱溶断シーラーは使用できず、高周波溶
断シーラー等の特殊な装置が必要であり、熱収縮応力も
高く、しかも該溶断シール部の機械的強度に前記ポリエ
チレン、ポリプロピレンの場合のような強靱性がないた
め破断し易く、引裂伝播現象も見られる他、上記溶断シ
ール時に悪臭を発生することもあり、好ましい包装材料
とは言えない。二軸延伸ポリプロピレンフィルムは、高
立体規則性ポリプロピレン樹脂が使用され、熱収縮後の
フィルムの透明性、光沢性に優れているため包装体の外
観がよく、商品価値を高める点で優れているものの、一
般的に熱収縮温度が高い、熱収縮温度巾が狭いため包装
加工条件範囲が狭い、フィルムの熱溶断シール強度が弱
い、熱収縮応力が高い性質を有するため被包装体の変
形、破壊も起こり易い、熱収縮時に熱収縮むら又は熱収
縮不完全部分(不完全収縮部分とも言え、溶断シール端
部、角隅部に特に発生し易く、その形状から通称ドッグ
イアーと言われている。以下、ドッグイアーと言う。)
が発生し易い等の欠点を有する。二軸延伸ポリエチレン
フィルムは、ポリエチレンの種類によりその特性は多種
多様であるが、概略、溶断シール温度が低い、溶断シー
ル部の高強度等の点で優れているものの、耐ブロッキン
グ性、透明性、衝撃強度、引裂強度等が上記ポリ塩化ビ
ニルとかポリプロピレンの場合に比して劣り、更に熱収
縮応力が比較的高い、熱収縮温度巾も狭く、しかも熱収
縮のための加熱による溶融破れを生じ易い他、収縮むら
に基づく引きつりや、あばた状凹凸が多く発生したり、
熱収縮包装後にドッグイアーがフィルム溶断シール部に
多発し易い等問題点も多い。Conventionally, as a heat-shrinkable film, a film obtained by biaxially stretching a film mainly made of polyethylene, polypropylene, or polyvinyl chloride is most commonly used. In the case of a biaxially stretched polyvinyl chloride film, although the transparency and glossiness of the film after heat shrinkage are excellent, a normal heat fusing sealer cannot be used, and special equipment such as a high frequency fusing sealer is required. , High heat shrinkage stress, and the mechanical strength of the fusing seal does not have toughness as in the case of polyethylene and polypropylene, so it is easy to break, tear propagation phenomenon is observed, and bad smell is generated at the time of fusing sealing. In some cases, this is not a preferable packaging material. The biaxially stretched polypropylene film uses a high stereoregularity polypropylene resin, and is excellent in transparency and glossiness of the film after heat shrinkage, so that the appearance of the package is good and the product value is high. Generally, the heat shrink temperature is high, the heat shrink temperature range is narrow, so the range of packaging processing conditions is narrow, the heat fusing seal strength of the film is weak, and the heat shrink stress is high, so deformation and destruction of the packaged object also occur. It is easy to occur, heat shrinkage unevenness during heat shrinkage or heat shrinkage incomplete portion (also referred to as incomplete shrinkage portion, which is particularly likely to occur at the end and corner of the fusing seal, and is generally called dog ear because of its shape. , Called dogear.)
Disadvantages such as easy occurrence of cracks. The biaxially stretched polyethylene film has various characteristics depending on the type of polyethylene, but generally has a low fusing seal temperature, is excellent in such points as a high strength of the fusing seal portion, but has excellent blocking resistance, transparency, Impact strength, tear strength, etc. are inferior to those of polyvinyl chloride or polypropylene, and the heat shrinkage stress is relatively high, the heat shrinkage temperature width is narrow, and the melt is easily broken by heating for heat shrinkage. In addition, pulling due to uneven shrinkage, pock-like irregularities often occur,
There are also many problems, such as dog ears tending to occur frequently in the film fusing seal after heat shrink packaging.
【0005】上記ポリエチレンの場合の問題点は、主と
してその重合触媒の進歩、改良によりかなり解消され、
しかも新しい優れた特性も付与された、多様化された熱
収縮性フィルムが出現しつつある。即ち、高圧法による
低密度ポリエチレン(LDPE)から、チーグラー触媒
やフィリップス触媒使用による中低圧の高密度ポリエチ
レン(HDPE)、線状低密度ポリエチレン(LLDP
E)、更にはメタロセン触媒使用による線状低密度ポリ
エチレン(LLDPE)へと発展、多様化したことはよ
く知られたことであるが、上記メタロセン触媒使用によ
る線状低密度ポリエチレンは、特に触媒の活性点が均
一であるシングルサイト触媒が使用されているため、ポ
リマーの分子量分布が狭いエチレンとコモノマーのα
−オレフィンとの重合が均一に行なわれるため、分子間
におけるモノマー成分比分布が狭いという特徴を有し、
フィルムのブロッキング性、低温シール性、透明性、衝
撃強度、引裂強度が大幅に改善され、他種樹脂との共押
出成形による熱収縮性多層フィルムも提案されている
(特開平7−314624号公報、同7−309962
号公報等)ものの、未だ熱収縮包装における熱収縮の適
性温度範囲が狭い、前記熱収縮包装時の収縮むら及びド
ッグイアーの発生は改善されておらず、未解決である。[0005] The above problems in the case of polyethylene are largely solved mainly by the progress and improvement of the polymerization catalyst.
Moreover, diversified heat-shrinkable films to which new excellent properties have been imparted are emerging. That is, from low-density polyethylene (LDPE) by a high-pressure method, to medium- and high-pressure high-density polyethylene (HDPE) using a Ziegler catalyst or a Phillips catalyst, and linear low-density polyethylene (LLDP).
E), and furthermore, it is well known that it has been developed and diversified to linear low density polyethylene (LLDPE) using a metallocene catalyst. Since a single-site catalyst with a uniform active site is used, the molecular weight distribution of the polymer is narrow, and the ethylene and comonomer α
-Since the polymerization with the olefin is carried out uniformly, the monomer component ratio distribution between molecules is narrow,
A heat-shrinkable multilayer film obtained by co-extrusion molding with another type of resin has been proposed, in which the blocking property, low-temperature sealing property, transparency, impact strength, and tear strength of the film are greatly improved (Japanese Patent Application Laid-Open No. Hei 7-314624). 7-309962
However, the temperature range suitable for heat shrinkage in heat shrink wrapping is still narrow, and the occurrence of uneven shrinkage and dog ear during the heat shrink wrapping has not been improved and is still unsolved.
【0006】[0006]
【発明が解決しようとする課題】本発明は、上記各種熱
収縮包装材料中、メタロセン触媒使用による線状低密度
ポリエチレン製の熱収縮性フィルムが、従来のポリエチ
レンフィルムの持つ低い溶断シール温度特性、熱収縮時
の溶断シール部の高強度特性を保持しつつ、しかもブロ
ッキング性、低温シール性、透明性、衝撃強度、引裂強
度の諸点において優れていることに着目し、これらの特
性を活かしつつ、熱収縮応力がより低く、ドッグイアー
の発生が少なく、且つ熱収縮温度範囲がより広い熱収縮
性ポリオレフィン系フィルムを提案することを課題とす
るものである。SUMMARY OF THE INVENTION The present invention relates to a heat-shrinkable film made of a linear low-density polyethylene using a metallocene catalyst in the above-mentioned various heat-shrinkable packaging materials. While maintaining the high strength properties of the fusing seal part during heat shrinkage, and paying attention to its excellent properties in terms of blocking properties, low-temperature sealing properties, transparency, impact strength, and tear strength, while utilizing these properties, An object of the present invention is to propose a heat-shrinkable polyolefin-based film having a lower heat shrinkage stress, less occurrence of dog ears, and a wider heat shrink temperature range.
【0007】[0007]
【課題を解決するための手段】本発明者らは、メタロセ
ン触媒使用による線状低密度ポリエチレン製の熱収縮性
フィルムを使用した熱収縮包装における熱収縮応力の低
下、熱収縮温度範囲の拡大について鋭意研究した結果、
特定の溶融流動性、分子量分布を兼ね備えた長鎖分岐構
造のポリオレフィンの層を有するフィルムが好適である
ことを見出し、本発明を完成した。Means for Solving the Problems The present inventors have proposed a method for reducing the heat shrinkage stress and expanding the heat shrinkage temperature range in a heat shrink wrapping using a heat shrinkable film made of linear low density polyethylene by using a metallocene catalyst. After extensive research,
The present inventors have found that a film having a polyolefin layer having a long-chain branched structure having both specific melt fluidity and molecular weight distribution is suitable, and completed the present invention.
【0008】即ち、本発明の要旨は以下の通りである。 (第1)メルトフロー比及び分子量比が (1)I10/I2 ≧5.63 (但し、I10は荷重10kg,温度190℃,10分間
あたりのメルトインデックスを、I2 は荷重2.16k
g,温度190℃,10分間あたりのメルトインデック
スをそれぞれ示す。) (2)Mw/Mn≦(I10/I2 )−4.63 (但し、Mwは重量平均分子量を、Mnは数平均分子量
をそれぞれ示す。) なる関係を満たし、長鎖分岐を持つポリオレフィンの層
を有する熱収縮性フィルム。 (第2)長鎖分岐を持つポリオレフィンが、エチレン−
1−オクテン共重合体である前記第1記載の熱収縮性フ
ィルム。 (第3)メルトフロー比及び密度が (1)5.63≦I10/I2 ≦15 (2)0.86≦d≦0.94 (但し、dは密度(g/cm3 )を示す。) なる関係を満たし、前記第1又は2記載の長鎖分岐を持
つポリオレフィンの層を有する熱収縮性フィルム。 (第4)前記第1ないし3のいずれかに記載の長鎖分岐
を持つポリオレフィンの層及びプロピレン系ポリマーの
層のいずれか一方を中間層とし、他を両外層とした3層
構造を有する熱収縮性フィルム。That is, the gist of the present invention is as follows. (1) Melt flow ratio and molecular weight ratio are (1) I 10 / I 2 ≧ 5.63 (where I 10 is a load index of 10 kg, temperature 190 ° C., melt index per 10 minutes, I 2 is a load index of 2. 16k
g, temperature 190 ° C., melt index per 10 minutes. (2) Mw / Mn ≦ (I 10 / I 2 ) −4.63 (where Mw represents a weight average molecular weight and Mn represents a number average molecular weight, respectively) Heat-shrinkable film having a layer of (Second) The polyolefin having a long chain branch is ethylene-
2. The heat-shrinkable film according to the above item 1, which is a 1-octene copolymer. (3) Melt flow ratio and density are (1) 5.63 ≦ I 10 / I 2 ≦ 15 (2) 0.86 ≦ d ≦ 0.94 (where d indicates density (g / cm 3 )) A heat-shrinkable film that satisfies the following relationship and has a polyolefin layer having a long-chain branch described in the first or second aspect. (4) A heat having a three-layer structure in which one of the polyolefin layer having a long-chain branch and the propylene-based polymer layer according to any one of the first to third aspects is an intermediate layer, and the other is both outer layers. Shrinkable film.
【0009】以下、本発明の内容を詳細に説明する。本
発明に係るポリオレフィンは、I10/I2 ≧5.63と規
定されるが、好ましくは5.63≦I10/I2 ≦15、よ
り好ましくは5.63≦I10/I2 ≦8.5なる範囲の値で
ある。ここにI10/I2 なるメルトフロー比は、流動性
測定条件を変えて測定した2つのメルトフロー値の比で
あり、流動性からみた分子量分布の目安になるものであ
る。I10/I2 が5.63未満であれば、成形加工性に劣
る。具体的には、高剪断応力下でメルトフラクチャー表
面性状を起こす点で問題がある。Hereinafter, the contents of the present invention will be described in detail. The polyolefin according to the present invention is defined as I 10 / I 2 ≧ 5.63, preferably 5.63 ≦ I 10 / I 2 ≦ 15, more preferably 5.63 ≦ I 10 / I 2 ≦ 8. .5. Here, the melt flow ratio of I 10 / I 2 is a ratio of two melt flow values measured under different fluidity measurement conditions, and is a measure of the molecular weight distribution from the viewpoint of fluidity. If I 10 / I 2 is less than 5.63, the moldability is poor. Specifically, there is a problem in that melt fracture surface properties occur under high shear stress.
【0010】又、本発明に係るポリオレフィンは、Mw
/Mn≦(I10/I2 )−4.63と規定されるが、1.5
≦〔Mw/Mn≦(I10/I2 )−4.63〕≦3がより
好ましい。ここにMw/Mnなる比は、重量平均分子量
と数平均分子量なる異種の測定法に基づく分子量の比で
あり、分子量分布の目安になるものである。Mw/Mn
>(I10/I2 )−4.63であれば、フィルムの光学特
性が劣る。具体的には、光沢度が低い、曇り度が高い等
の点で問題がある。The polyolefin according to the present invention has Mw
/ Mn ≦ (I 10 / I 2 ) −4.63, but 1.5
≦ [Mw / Mn ≦ (I 10 / I 2 ) −4.63] ≦ 3 is more preferable. Here, the ratio of Mw / Mn is a ratio of the molecular weight based on different measuring methods, that is, the weight average molecular weight and the number average molecular weight, and serves as a standard of the molecular weight distribution. Mw / Mn
If> (I 10 / I 2 ) −4.63, the optical characteristics of the film are inferior. Specifically, there is a problem in that glossiness is low and haze is high.
【0011】更に本発明に係るポリオレフィンの密度は
0.86g/cm3 以上,0.94g/cm3 以下あること
が好ましいが、より好ましくは0.86g/cm3 以上,
0.91g/cm3 以下、更に好ましくは0.86g/cm
3 以上,0.89g/cm3 以下である。密度が0.86g
/cm3 未満の場合は、フィルム表面がべたつき易くな
る点で好ましくない。又、0.94g/cm3 を超えると
成形加工性に劣る点で好ましくない。Further, the density of the polyolefin according to the present invention is
It is preferably 0.86 g / cm 3 or more and 0.94 g / cm 3 or less, more preferably 0.86 g / cm 3 or more.
0.91 g / cm 3 or less, more preferably 0.86 g / cm 3
3 or more and 0.89 g / cm 3 or less. 0.86g density
If it is less than / cm 3 , it is not preferable because the film surface becomes sticky. On the other hand , if it exceeds 0.94 g / cm 3 , it is not preferable because moldability is poor.
【0012】本発明に規定する「長鎖分岐を持つポリオ
レフィン」とは「ポリマーのバックボーンが、炭素数1
000個あたり、0.01〜3個の長分岐鎖によって置換
されているもの」を指すが、この数は好ましくは0.01
〜1個であり、更に好ましくは0.05〜1個である。こ
の長鎖分岐を持つポリオレフィンとしては、エチレンと
α−オレフィン共重合体が好ましく、またα−オレフィ
ンとしては1−ブテン、1−ヘキセン、2−メチル−1
−ペンテン、1−オクテンが好ましく、特に1−オクテ
ンが好ましく使用される。コモノマーとして上記のよう
なα−オレフィンを用い、長鎖分岐を形成することによ
り、前記I10/I2 及びMw/Mnの値を所望の範囲に
規定することができ、後記のごとく広い熱収縮性温度範
囲を付与することができ、また、熱収縮応力の低下を図
ることができる。The term "polyolefin having a long-chain branch" as defined in the present invention means that the backbone of the polymer has 1 carbon atom.
Per 000 are substituted by 0.01 to 3 long-branched chains ", but this number is preferably 0.01
, And more preferably 0.05 to 1. As the polyolefin having a long chain branch, ethylene and an α-olefin copolymer are preferable, and as the α-olefin, 1-butene, 1-hexene, 2-methyl-1
-Pentene and 1-octene are preferred, and 1-octene is particularly preferably used. By using the above-mentioned α-olefin as a comonomer and forming a long-chain branch, the values of I 10 / I 2 and Mw / Mn can be specified in desired ranges, and a wide heat shrinkage can be obtained as described later. Temperature range can be given, and the heat shrinkage stress can be reduced.
【0013】本発明に規定する「長鎖分岐を持つポリオ
レフィンを使用した熱収縮性フィルム」は、上記特定の
ポリオレフィンを使用し、公知の製造方法及び加工方法
によりフラット又は管状フィルムを製造した後、テンタ
ー方式、インフレーション方式又はチューブラー方式に
より、同時又は逐次二軸延伸する方法が最も好適であ
る。なお、高い熱収縮性を付与するためには、延伸速度
は可及的高速で行い、延伸温度は可及的低温で行なうこ
とが好ましく、また延伸処理後の急冷処理が好ましく採
用される。もっとも、熱収縮性の程度の調節のために、
延伸処理後に適宜アニール処理をしてもよい。The "heat-shrinkable film using a polyolefin having a long-chain branch" defined in the present invention is obtained by producing a flat or tubular film by a known production method and processing method using the above-mentioned specific polyolefin. A method of simultaneous or sequential biaxial stretching by a tenter method, an inflation method or a tubular method is most preferable. In order to impart high heat shrinkability, the stretching speed is preferably as high as possible, the stretching temperature is preferably as low as possible, and quenching after the stretching is preferably employed. However, to adjust the degree of heat shrinkage,
After the stretching process, an annealing process may be appropriately performed.
【0014】本発明に係るポリオレフィン樹脂には、成
形用添加材として一般的に知られているアンチブロッキ
ング剤、滑剤、帯電防止剤、核剤、延伸配向剤、酸化防
止剤、熱安定剤、光安定剤、難燃剤、顔料、充填剤、相
溶化剤等を適宜添加することができる。[0014] The polyolefin resin according to the present invention includes an antiblocking agent, a lubricant, an antistatic agent, a nucleating agent, a stretching orientation agent, an antioxidant, a heat stabilizer, a light stabilizer which is generally known as a molding additive. Stabilizers, flame retardants, pigments, fillers, compatibilizers and the like can be added as appropriate.
【0015】本発明に係る熱収縮性フィルムは、その熱
収縮特性を阻害しない限り、機械的強度、溶断シール強
度、包装適性等の向上の要求に応じて、上記特定のポリ
オレフィン樹脂製フィルムに、延伸又は無延伸状態の合
成樹脂層を積層した複合フィルムとして使用することが
できるが、ポリプロピレン系樹脂又はそのフィルムとの
複合フィルムが耐熱性の点で特に好ましい。上記ポリプ
ロピレン系樹脂又はそのフィルムとの複合フィルムは、
本発明に係る熱収縮性ポリオレフィンの層を中間層とす
る3層構造を含むもの、又は該熱収縮性ポリオレフィン
の層を両外層とし、中間層としてポリプロピレン系樹脂
又はそのフィルムを配した3層構造を含むものが、加熱
収縮処理時の耐熱性、低い熱収縮応力、熱収縮処理温度
範囲の拡大化の点で特に好ましい。The heat-shrinkable film according to the present invention can be used in the above-mentioned specific polyolefin resin film in accordance with demands for improvement in mechanical strength, fusing seal strength, packaging suitability, etc., as long as the heat-shrinkable property is not impaired. Although it can be used as a composite film in which a stretched or non-stretched synthetic resin layer is laminated, a polypropylene-based resin or a composite film with the film is particularly preferable in terms of heat resistance. The composite film with the polypropylene-based resin or a film thereof,
One having a three-layer structure in which the heat-shrinkable polyolefin layer according to the present invention is an intermediate layer, or a three-layer structure in which the heat-shrinkable polyolefin layer is used as both outer layers, and a polypropylene-based resin or a film thereof is arranged as the intermediate layer. Is particularly preferred in terms of heat resistance during heat shrink treatment, low heat shrinkage stress, and expansion of the heat shrink treatment temperature range.
【0016】なお、前記他の合成樹脂としては、上記ポ
リプロピレン系樹脂の他に低密度ポリエチレン、線状低
密度ポリエチレン、高密度ポリエチレン、エチレン−酢
酸ビニル共重合体、エチレン−メチルメタクリレート共
重合体、エチレン−メチルアクリレート共重合体、エチ
レン−アクリル酸共重合体の金属塩等のアイオノマー、
石油樹脂等を挙げることができる。なお積層される当該
他の合成樹脂は延伸フィルム、又は未延伸フィルムとし
て本発明に係るポリオレフィン系の熱収縮フィルムに複
合化してもよいが、未延伸フィルムと本発明に係るポリ
オレフィンの未延伸フィルムを積層した後、同時に延伸
処理し、熱収縮性付与処理をしてもよい。更に、これら
多層構造のフィルムは、通常の方法で複数枚のフィルム
の積層加工で製造される他、本発明に係るポリオレフィ
ン系フィルム表面に上記各種樹脂を溶融積層する方法で
も製造される。The other synthetic resins include low density polyethylene, linear low density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, ethylene-methyl methacrylate copolymer, Ionomers such as ethylene-methyl acrylate copolymers and metal salts of ethylene-acrylic acid copolymers,
Petroleum resins and the like can be mentioned. The other synthetic resin to be laminated may be a stretched film, or may be compounded into the polyolefin-based heat-shrinkable film according to the present invention as an unstretched film. After lamination, a stretching treatment may be performed at the same time to perform a heat shrinkability imparting treatment. Further, these films having a multilayer structure are produced by laminating a plurality of films by an ordinary method, and also by a method of melting and laminating the above various resins on the surface of the polyolefin film according to the present invention.
【0017】[0017]
【実施例】以下、本発明を実施例を用いて説明する。 (実施例1)3層構造の複合フィルムの中間層形成用樹
脂として、I10/I2 が9.8,Mw/Mnが2.2, 密度
が0.902g/cm3 のエチレン−1−オクテン共重合
体10重量部と、エチレン含有量が2.3重量%のエチレ
ン−プロピレン共重合体90重量部とからなる樹脂組成
物を、両外層形成用樹脂として、I10/I2 が9.8,M
w/Mnが2.2,密度が0.902g/cm3 のエチレン
−1−オクテン共重合体を使用してそれぞれ使用し、3
層共押出成形用であって240℃に設定されたサーキュ
ラーダイスに連結設置された3台の押出機に供給し、層
厚み比が1(外層):2(中間層):1(外層)となる
ように押出し、水冷方式により急冷して延伸用原反管状
シートを成形した。次に該管状シートを炉の温度400
℃の管状遠赤外線炉内を通過させて加熱しつつチューブ
ラー延伸法により、縦方向、横方向共に5倍に延伸し、
直ちに空冷方式により急冷して厚さ12μmの熱収縮性
の二軸延伸フィルムを得た。上記得られたフィルムの最
大熱収縮応力は16kg/cm2 と低い値であった。収
縮率が5%及び30%をそれぞれ示す温度の差 (以下、
収縮温度巾という)は39℃と広く、所望の収縮特性を
容易に得ることができることがわかった。次に、熱収縮
性フィルムで20cm(巾)×40cm(長)×5cm(厚)
のボール紙箱(紙厚み1mm)を包装し、収縮トンネル温
度150℃に設定したシュリンク包装機内を通して熱収
縮包装テストを行なったところ、ボール箱には変形は全
く見られず、フィルム全面が緊張した平滑な包装状態が
得られ、溶断シール部の端部とか被包装体から最も離れ
た溶断シール部分に通常生じやすいドッグイアーは見ら
れなかった。収縮トンネル温度を上記温度よりも更に2
0〜30℃高くして同様の収縮包装テストを行なった。
フィルム面のうち、被包装物と接触していない部分によ
く見られる溶融破れ、白化現象も見られず、又溶断シー
ル部に設けた空気抜き孔とか該シール部分における破袋
現象も全く発生しなかった。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to embodiments. As an intermediate layer forming resin of the composite film (Example 1) 3-layer structure, I 10 / I 2 is 9.8, Mw / Mn of 2.2, a density of 0.902 g / cm 3 Ethylene-1- and octene copolymer 10 parts by weight, an ethylene content of 2.3 wt% ethylene - a resin composition comprising a propylene copolymer 90 parts by weight, as the both outer layers forming resin, I 10 / I 2 is 9 .8, M
Using an ethylene-1-octene copolymer having a w / Mn of 2.2 and a density of 0.902 g / cm 3 ,
It is supplied to three extruders connected to a circular die set at 240 ° C. for layer coextrusion molding, and the layer thickness ratio is 1 (outer layer): 2 (intermediate layer): 1 (outer layer). The resulting sheet was extruded and quenched by a water cooling method to form a raw tubular sheet for stretching. The tubular sheet is then heated to a furnace temperature of 400.
℃ 5 times in both the vertical and horizontal directions by tubular stretching while heating by passing through a tubular far-infrared furnace at
Immediately by an air cooling method, a heat-shrinkable biaxially stretched film having a thickness of 12 μm was obtained. The maximum heat shrinkage stress of the obtained film was a low value of 16 kg / cm 2 . The difference between the temperatures at which the shrinkage rate shows 5% and 30%, respectively (hereinafter,
(Referred to as shrinkage temperature width) is as wide as 39 ° C., and it was found that desired shrinkage characteristics can be easily obtained. Next, a heat-shrinkable film of 20 cm (width) x 40 cm (length) x 5 cm (thick)
Was packed in a cardboard box (paper thickness 1 mm) and subjected to a heat shrink wrap test through a shrink wrapping machine set at a shrink tunnel temperature of 150 ° C. A good packaging condition was obtained, and no dog ears, which are usually generated at the end of the fusing seal portion or the fusing seal portion furthest from the packaged object, were observed. Reduce the shrink tunnel temperature by 2 more than the above temperature.
A similar shrink wrap test was performed at 0-30 ° C.
Of the film surface, there is no melting tearing and whitening phenomenon often seen in the portion not in contact with the packaged object, and no air vent hole provided in the fusing seal portion or no bag breaking phenomenon at the sealing portion. Was.
【0018】(実施例2)実施例1における中間層形成
用樹脂としてMIが8,密度が0.85/cm3 ,ビカッ
ト軟化点が94℃のプロピレン−エチレン−ブテン共重
合体を使用し、層厚み比を35(外層):30(中間
層):35(外層)とした以外は実施例1と同様の条件
で厚み10μmの熱収縮性の二軸延伸フィルムを得た。
次に、実施例1同様の条件で各種特性を測定した。上記
二軸延伸フィルムの最大熱収縮応力は20kg/cm2
と低い値であり、収縮温度巾は44℃と広く、所望の収
縮特性を容易に得ることができることがわかった。更
に、熱収縮包装テストを行なったところ、ボール箱には
変形は全く見られず、フィルム全面が緊張した平滑な包
装状態が得られ、溶断シール部にはドッグイアーは全く
見られなかった。収縮トンネル温度を更に高くした収縮
包装テストにおいては、フィルム面のうち、被包装物と
の非接触部分での溶融破れ、白化現象も見られず、又溶
断シール部における破袋現象も全く発生しなかった。Example 2 A propylene-ethylene-butene copolymer having an MI of 8, a density of 0.85 / cm 3 and a Vicat softening point of 94 ° C. was used as a resin for forming an intermediate layer in Example 1, A heat-shrinkable biaxially stretched film having a thickness of 10 μm was obtained under the same conditions as in Example 1 except that the layer thickness ratio was changed to 35 (outer layer): 30 (intermediate layer): 35 (outer layer).
Next, various characteristics were measured under the same conditions as in Example 1. The maximum heat shrinkage stress of the biaxially stretched film is 20 kg / cm 2
It was found that the shrinkage temperature range was as wide as 44 ° C., and that desired shrinkage characteristics could be easily obtained. Further, when a heat shrinkage packaging test was performed, no deformation was observed in the cardboard box, a smooth packaging state in which the entire surface of the film was tensioned was obtained, and no dog ear was observed in the fusing seal portion. In the shrink wrapping test with the shrink tunnel temperature further increased, no melting and tearing and no whitening were observed in the non-contact portion of the film surface with the packaged object, and there was no bag breaking at the fusing seal. Did not.
【0019】(実施例3)3層構造の複合フィルムの中
間層形成用樹脂として、I10/I2 が7.9,Mw/Mn
が2.0, 密度が0.870g/cm3 のエチレン−1−オ
クテン共重合体を、両外層形成用樹脂として、密度が0.
920g/cm3 のエチレン−1−オクテン共重合体を
それぞれ使用し、3層共押出成形用であって230℃に
設定されたTダイに連結設置された3台の押出機に供給
し、層厚み比が1(外層):2(中間層):1(外層)
となるように押出し、延伸用原反シートを成形した。次
に該シートをテーブルテンターを用いて延伸温度105
℃にて縦方向、横方向同時に延伸し、厚さ12μmの熱
収縮性のフィルムを得た。次に、実施例1同様の条件で
各種特性を測定した。上記二軸延伸フィルムの最大熱収
縮応力は21kg/cm2 と低い値であり、収縮温度巾
は25℃と広く、所望の収縮特性を容易に得ることがで
きることがわかった。更に、熱収縮包装テストを行なっ
たところ、ボール箱には変形は全く見られず、フィルム
全面が緊張した平滑な包装状態が得られ、溶断シール部
にはドッグイアーは全く見られなかった。収縮トンネル
温度を更に高くした収縮包装テストにおいては、フィル
ム面のうち、被包装物との非接触部分での溶融破れ、白
化現象も見られず、又溶断シール部における破袋現象も
全く発生しなかった。Example 3 As a resin for forming an intermediate layer of a composite film having a three-layer structure, I 10 / I 2 is 7.9, Mw / Mn.
Is 2.0 and a density of 0.870 g / cm 3 is used as a resin for forming both outer layers.
920 g / cm 3 of ethylene-1-octene copolymer was used and supplied to three extruders connected to a T-die set at 230 ° C. for three-layer coextrusion molding. The thickness ratio is 1 (outer layer): 2 (middle layer): 1 (outer layer)
Then, a raw sheet for stretching was formed. Next, the sheet was stretched at a stretching temperature of 105 using a table tenter.
The film was simultaneously stretched in the machine direction and the transverse direction at ℃ to obtain a heat-shrinkable film having a thickness of 12 μm. Next, various characteristics were measured under the same conditions as in Example 1. The maximum heat shrinkage stress of the biaxially stretched film was a low value of 21 kg / cm 2 , and the shrinkage temperature range was as wide as 25 ° C., indicating that desired shrinkage characteristics could be easily obtained. Further, when a heat shrinkage packaging test was performed, no deformation was observed in the cardboard box, a smooth packaging state in which the entire surface of the film was tensioned was obtained, and no dog ear was observed in the fusing seal portion. In the shrink wrapping test with the shrink tunnel temperature further increased, no melting and tearing and no whitening were observed in the non-contact portion of the film surface with the packaged object, and there was no bag breaking at the fusing seal. Did not.
【0020】(実施例4)実施例3における両外層形成
用樹脂として、I10/I2 が9.8,Mw/Mnが2.2,
密度が0.902g/cm3 のエチレン−1−オクテン共
重合体を使用した以外は実施例3と同様にして、層厚み
比が1(外層):1.5(中間層):1(外層)の延伸用
原反シートを成形した。延伸温度を97℃とした以外は
実施例3と同様の方法で延伸し、厚さ15μmの熱収縮
性のフィルムを得た。次に、熱収縮包装テストの収縮ト
ンネル温度を135℃とした以外は実施例1と同様の条
件で各種特性を測定した。上記二軸延伸フィルムの最大
熱収縮応力は17kg/cm2 と低い値であり、収縮温
度巾は26℃と広く、所望の収縮特性を容易に得ること
ができることがわかった。更に、熱収縮包装テストを行
なったところ、ボール箱には変形は全く見られず、フィ
ルム全面が緊張した平滑な包装状態が得られ、溶断シー
ル部にはドッグイアーは全く見られなかった。収縮トン
ネル温度を更に高くした収縮包装テストにおいては、フ
ィルム面のうち、被包装物との非接触部分での溶融破
れ、白化現象も見られず、又溶断シール部における破袋
現象も全く発生しなかった。(Example 4) As the resin for forming both outer layers in Example 3, I 10 / I 2 was 9.8, Mw / Mn was 2.2,
A layer thickness ratio was 1 (outer layer): 1.5 (intermediate layer): 1 (outer layer) in the same manner as in Example 3 except that an ethylene-1-octene copolymer having a density of 0.902 g / cm 3 was used. ) Was formed. The film was stretched in the same manner as in Example 3 except that the stretching temperature was 97 ° C., to obtain a heat-shrinkable film having a thickness of 15 μm. Next, various characteristics were measured under the same conditions as in Example 1 except that the shrink tunnel temperature in the heat shrink packaging test was set to 135 ° C. The maximum heat shrinkage stress of the biaxially stretched film was a low value of 17 kg / cm 2 , and the shrinkage temperature range was as wide as 26 ° C., indicating that desired shrinkage characteristics could be easily obtained. Further, when a heat shrinkage packaging test was performed, no deformation was observed in the cardboard box, a smooth packaging state in which the entire surface of the film was tensioned was obtained, and no dog ear was observed in the fusing seal portion. In the shrink wrapping test with the shrink tunnel temperature further increased, no melting and tearing and no whitening were observed in the non-contact portion of the film surface with the packaged object, and there was no bag breaking at the fusing seal. Did not.
【0021】(実施例5)実施例3における中間層形成
用樹脂として、I10/I2 が11,Mw/Mnが2.3,
密度が0.895g/cm3 のエチレン−1−オクテン共
重合体を使用した以外は実施例3と同様にして、層厚み
比が1(外層):3(中間層):1(外層)の延伸用原
反シートを成形した。延伸温度を96℃とした以外は実
施例3と同様の方法で延伸し、厚さ20μmの熱収縮性
のフィルムを得た。次に、熱収縮包装テストの収縮トン
ネル温度を135℃とした以外は実施例1と同様の条件
で各種特性を測定した。上記二軸延伸フィルムの最大熱
収縮応力は16kg/cm2 と低い値であり、収縮温度
巾は23℃と広く、所望の収縮特性を容易に得ることが
できることがわかった。更に、熱収縮包装テストを行な
ったところ、ボール箱には変形は全く見られず、フィル
ム全面が緊張した平滑な包装状態が得られ、溶断シール
部にはドッグイアーは全く見られなかった。収縮トンネ
ル温度を更に高くした収縮包装テストにおいては、フィ
ルム面のうち、被包装物との非接触部分での溶融破れ、
白化現象も見られず、又溶断シール部における破袋現象
も全く発生しなかった。(Example 5) As a resin for forming an intermediate layer in Example 3, I 10 / I 2 is 11, Mw / Mn is 2.3,
A layer thickness ratio of 1 (outer layer): 3 (intermediate layer): 1 (outer layer) was obtained in the same manner as in Example 3 except that an ethylene-1-octene copolymer having a density of 0.895 g / cm 3 was used. A raw sheet for stretching was formed. The film was stretched in the same manner as in Example 3 except that the stretching temperature was 96 ° C., to obtain a heat-shrinkable film having a thickness of 20 μm. Next, various characteristics were measured under the same conditions as in Example 1 except that the shrink tunnel temperature in the heat shrink packaging test was set to 135 ° C. The maximum heat shrinkage stress of the biaxially stretched film was a low value of 16 kg / cm 2 , and the shrinkage temperature range was as wide as 23 ° C., indicating that desired shrinkage characteristics could be easily obtained. Further, when a heat shrinkage packaging test was performed, no deformation was observed in the cardboard box, a smooth packaging state in which the entire surface of the film was tensioned was obtained, and no dog ear was observed in the fusing seal portion. In the shrink wrap test with the shrink tunnel temperature even higher, the film surface melts and breaks at the non-contact portion with the packaged object,
No whitening phenomenon was observed, and no bag breaking phenomenon occurred at the fusing seal portion.
【0022】(比較例1)実施例1における中間層形成
用樹脂及び両外層形成用樹脂として、エチレン含有量が
2.3重量%のエチレン−プロピレン共重合体を使用した
以外、実施例1と同様の条件で、厚み12μmの熱収縮
性の二軸延伸フィルムを得た。実施例1同様にして、得
られたフィルムの各種特性を測定した。最大熱収縮応力
は40kg/cm2 と極めて高い値であり、収縮温度巾
は19℃と極めて狭いことがわかった。次に、収縮トン
ネル温度を150℃、155℃及び160℃でそれぞ
れ、実施例1と同様にして熱収縮包装テストを行なった
ところ、160℃で初めて熱収縮を伴った収縮包装をす
ることができたが、溶断シール部の端部に大きなドッグ
イアーが発生した他、フィルム表面の一部に皺が見ら
れ、包装仕上がり状態としてはよくなかった。収縮トン
ネル温度を160℃よりも更に5〜10℃高くして同様
の熱収縮包装テストを行なったところ、溶断シール部及
び空気抜き孔部分に破袋現象が観察された。Comparative Example 1 The resin for forming the intermediate layer and the resin for forming both outer layers in Example 1 had an ethylene content of
A heat-shrinkable biaxially stretched film having a thickness of 12 μm was obtained under the same conditions as in Example 1 except that 2.3% by weight of the ethylene-propylene copolymer was used. Various properties of the obtained film were measured in the same manner as in Example 1. The maximum heat shrinkage stress was an extremely high value of 40 kg / cm 2 , and the shrinkage temperature width was found to be extremely narrow at 19 ° C. Next, a heat shrink wrapping test was performed at 150 ° C., 155 ° C., and 160 ° C., respectively, in the same manner as in Example 1, and shrink wrapping with heat shrinkage was possible at 160 ° C. for the first time. However, a large dog ear was generated at the end of the fusing seal portion, wrinkles were observed on a part of the film surface, and the finished packaging was not good. When the same heat shrink wrapping test was performed with the shrink tunnel temperature further raised from 5 ° C. to 10 ° C. than 160 ° C., a bag breaking phenomenon was observed at the fusing seal portion and the air vent hole portion.
【0023】(比較例2)比較例1における中間層形成
用樹脂として、I10/I2 が5.60,Mw/Mnが2.
0,密度が0.880g/cm3 のエチレン−1−ブテン
共重合体を使用した以外、実施例1と同様の条件で、厚
み12μmの二軸延伸フィルムを得た。得られたフィル
ムの最大熱収縮応力は43kg/cm2 と非常に高い値
であり、収縮温度巾は15℃と非常に狭いことがわかっ
た。次に、収縮トンネル温度を155℃とした以外実施
例1と同様にして収縮包装テストを行なったところ、収
縮包装をすることはできたが、溶断シール部の端部に大
きなドッグイアーが発生した他、フィルム表面の一部に
あばた状の凹凸が見られ、包装仕上がり状態としてはよ
くなかった。収縮トンネル温度を更に5〜10℃高くし
て同様の収縮包装テストを行なったところ、溶断シール
部及び空気抜き孔部分に破袋現象が観察された。Comparative Example 2 As the resin for forming the intermediate layer in Comparative Example 1, I 10 / I 2 was 5.60 and Mw / Mn was 2.60.
A biaxially stretched film having a thickness of 12 μm was obtained under the same conditions as in Example 1 except that an ethylene-1-butene copolymer having a density of 0.880 g / cm 3 was used. The maximum heat shrinkage stress of the obtained film was a very high value of 43 kg / cm 2 , and the shrinkage temperature range was found to be very narrow at 15 ° C. Next, a shrink wrap test was performed in the same manner as in Example 1 except that the shrink tunnel temperature was set to 155 ° C., but shrink wrap was possible, but a large dog ear was generated at the end of the fusing seal portion. In addition, pock-like irregularities were observed on a part of the film surface, and the finished packaging was not good. When a similar shrink packaging test was performed by further increasing the shrink tunnel temperature by 5 to 10 ° C., a bag break phenomenon was observed at the fusing seal portion and the air vent hole portion.
【0024】(比較例3)比較例1における中間層形成
用樹として、I10/I2 が5.50,Mw/Mnが2.3,
密度が0.912g/cm3 のエチレン−1−ブテン共重
合体を使用した以外、実施例1と同様の条件で、厚み1
2μmの二軸延伸フィルムを得た。得られたフィルムの
最大熱収縮応力は42kg/cm2 と非常に高い値であ
り、収縮温度巾は12℃と非常に狭いことがわかった。
更に、収縮トンネル温度を155℃とした以外実施例1
と同様にして収縮包装テストを行なったところ、収縮包
装をすることはできたが、溶断シールの交差した角部に
大きなドッグイアーが発生した他、被包装体の角部近傍
のフィルムに引きつり状皺が見られ、包装仕上がり状態
としてはよくなかった。収縮トンネル温度を更に5〜1
0℃高くして同様の収縮包装テストを行なったところ、
溶断シール部及び空気抜き孔部分に破袋現象が観察され
た。Comparative Example 3 As a tree for forming an intermediate layer in Comparative Example 1, I 10 / I 2 was 5.50, Mw / Mn was 2.3,
Except for using an ethylene-1-butene copolymer having a density of 0.912 g / cm 3 , a thickness of 1 was obtained under the same conditions as in Example 1.
A 2 μm biaxially stretched film was obtained. The maximum heat shrinkage stress of the obtained film was a very high value of 42 kg / cm 2 , and the shrinkage temperature range was found to be very narrow at 12 ° C.
Further, Example 1 except that the shrink tunnel temperature was set to 155 ° C.
When the shrink wrap test was performed in the same manner as above, shrink wrap could be performed, but a large dog ear was generated at the corner where the fusing seal crossed, and the film was pulled on the film near the corner of the packaged object. Wrinkles were observed and the finished packaging was not good. Further reduce the shrink tunnel temperature by 5 to 1
When the same shrink packaging test was performed at 0 ° C higher,
A bag breaking phenomenon was observed in the fusing seal portion and the air vent hole portion.
【0025】[0025]
【発明の効果】特定のメルトフロー比(I10/I2 )及
び特定のMw/Mnを兼ね備えた、長鎖分岐を持つポリ
オレフィンを単層フィルムとして、又は3層構造におけ
る中間層又は両外層とした複層構造を含む多層フィルム
は、低熱収縮応力、広い熱収縮温度巾、溶断シール部の
高強度、いわゆるドッグイアーが発生しない点で優れて
いることがわかった。According to the present invention, a polyolefin having a specific melt flow ratio (I 10 / I 2 ) and a specific Mw / Mn and having a long chain branch is used as a single-layer film, or as an intermediate layer or both outer layers in a three-layer structure. It was found that the multilayer film having the multilayer structure was excellent in low heat shrinkage stress, wide heat shrinkage temperature range, high strength of the fusing seal portion, that is, so-called dog ear was not generated.
Claims (4)
あたりのメルトインデックスを、I2 は荷重2.16k
g,温度190℃,10分間あたりのメルトインデック
スをそれぞれ示す。) (2)Mw/Mn≦(I10/I2 )−4.63 (但し、Mwは重量平均分子量を、Mnは数平均分子量
をそれぞれ示す。) なる関係を満たし、長鎖分岐を持つポリオレフィンの層
を有する熱収縮性フィルム。The melt flow ratio and the molecular weight ratio are as follows: (1) I 10 / I 2 ≧ 5.63 (where I 10 is a load index of 10 kg, temperature 190 ° C., melt index per 10 minutes, I 2 is a load index of 2 .16k
g, temperature 190 ° C., melt index per 10 minutes. (2) Mw / Mn ≦ (I 10 / I 2 ) −4.63 (where Mw represents a weight average molecular weight and Mn represents a number average molecular weight, respectively) Heat-shrinkable film having a layer of
ン−1−オクテン共重合体である請求項1記載の熱収縮
性フィルム。2. The heat-shrinkable film according to claim 1, wherein the polyolefin having a long chain branch is an ethylene-1-octene copolymer.
つポリオレフィンの層を有する熱収縮性フィルム。3. The melt flow ratio and the density are as follows: (1) 5.63 ≦ I 10 / I 2 ≦ 15 (2) 0.86 ≦ d ≦ 0.94 (where d is the density (g / cm 3 )) A heat-shrinkable film which satisfies the following relationship and has a layer of a polyolefin having long-chain branching according to claim 1 or 2.
分岐を持つポリオレフィンの層及びプロピレン系ポリマ
ーの層のいずれか一方を中間層とし、他を両外層とした
3層構造を有する熱収縮性フィルム。4. A three-layer structure in which one of the polyolefin layer having a long chain branch and the propylene-based polymer layer according to any one of claims 1 to 3 is an intermediate layer, and the other is both outer layers. Heat shrinkable film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8274390A JPH10119211A (en) | 1996-10-17 | 1996-10-17 | Heat-shrinkable film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8274390A JPH10119211A (en) | 1996-10-17 | 1996-10-17 | Heat-shrinkable film |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10119211A true JPH10119211A (en) | 1998-05-12 |
Family
ID=17541009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8274390A Pending JPH10119211A (en) | 1996-10-17 | 1996-10-17 | Heat-shrinkable film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10119211A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7235607B2 (en) | 2002-09-05 | 2007-06-26 | Exxonmobil Chemical Patents Inc. | Shrink film |
| US7951873B2 (en) | 2006-05-05 | 2011-05-31 | Exxonmobil Chemical Patents Inc. | Linear low density polymer blends and articles made therefrom |
-
1996
- 1996-10-17 JP JP8274390A patent/JPH10119211A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7235607B2 (en) | 2002-09-05 | 2007-06-26 | Exxonmobil Chemical Patents Inc. | Shrink film |
| US7951873B2 (en) | 2006-05-05 | 2011-05-31 | Exxonmobil Chemical Patents Inc. | Linear low density polymer blends and articles made therefrom |
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