JPH01253445A - Multilayer heat shrinkable film - Google Patents

Multilayer heat shrinkable film

Info

Publication number
JPH01253445A
JPH01253445A JP63082066A JP8206688A JPH01253445A JP H01253445 A JPH01253445 A JP H01253445A JP 63082066 A JP63082066 A JP 63082066A JP 8206688 A JP8206688 A JP 8206688A JP H01253445 A JPH01253445 A JP H01253445A
Authority
JP
Japan
Prior art keywords
layer
resin
core layer
heat
polypropylene resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP63082066A
Other languages
Japanese (ja)
Other versions
JP2641242B2 (en
Inventor
Kazuo Kondo
和夫 近藤
Shinya Ishiguro
石黒 信也
Toyoki Wano
和納 豊喜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Okura Industrial Co Ltd
Original Assignee
Okura Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Okura Industrial Co Ltd filed Critical Okura Industrial Co Ltd
Priority to JP63082066A priority Critical patent/JP2641242B2/en
Publication of JPH01253445A publication Critical patent/JPH01253445A/en
Priority to US07/584,635 priority patent/US5086266A/en
Application granted granted Critical
Publication of JP2641242B2 publication Critical patent/JP2641242B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

PURPOSE:To obtain a multilayer heat shrinkable film having excellent heat shrinkability at low temperatures, excellent heat shrinking package adaptability temperature range, preferable slipperiness, optical properties, and excellent melt sealability by providing a shielding layer between an outermost layer and a core layer. CONSTITUTION:There is obtained a tubular coextruded multilayer unoriented original sheet having both outermost layers made of crystalline polypropylene resin having 135-150 deg.C of melting point, a core layer made of normal chain low density polyethylene resin having 0.890-0.910g/cm<3> of density and 60-80 deg.C of Vicat softening point, a shielding layer made of a resin composition in which the crystalline polypropylene resin used for both the outermost layers and the polyethylene resin used as the core layer are mixed by weight in a range of 2:1-3:1, and a structure of the outermost layer, the shielding layer, the core layer, the shielding layer and the outermost layer. The thickness of the shielding layer ranges from 1-30% of the whole thickness, and the melt flow index (MI) of the crystalline polypropylene resin is higher than that of the low density polypropylene resin. Lubricant and antiblocking agent are added to the outermost layers and the same lubricant as that of both the outermost layers is added to the core layer and the shielding layer.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明の多層熱収縮性フィルムは、商品をラフに包んで
おき、これを加熱装置(収縮トンネル)によって加熱収
縮させ、タイトな包装を行なう方式の熱収縮包装に用い
るものである。そして、カップ食品、乳酸菌飲料品、紙
パツク飲料品、冷凍・冷蔵食品、医薬品、エアゾール缶
、或は、文具・玩具等の日用品の熱収縮包装に利用され
、特に、集積包装や改ざん防止包装に優れた効果を発揮
するものである。
[Detailed Description of the Invention] (Industrial Application Field) The multilayer heat-shrinkable film of the present invention can be used to roughly wrap a product and heat-shrink it using a heating device (shrink tunnel) to achieve tight packaging. This method is used for heat shrink packaging. It is used for heat shrink packaging of cup foods, lactic acid bacteria beverages, paper packaged beverages, frozen/refrigerated foods, pharmaceuticals, aerosol cans, and daily necessities such as stationery and toys. It is especially suitable for stacking packaging and tamper-proof packaging. It exhibits excellent effects.

〈従来の技術) 従来より、熱収縮包装分野に利用されている熱収縮性フ
ィルムとしては、ポリエチレン樹脂やポリプロピレン樹
脂、或は、ポリ塩化ビニル樹脂等からなる、種々のフィ
ルムがあり、しかも、数多く市販されている。中ても、
ポリプロピレン樹脂よりなる熱収縮性フィルムは、その
本来有している透明性、光沢、防湿性、或は、無公害性
等の優れた特性によって広く一般に利用されている。し
かし、ポリプロピレン樹脂からなる熱収縮性フィルムは
、ポリ塩化ビニル樹脂等からなる熱収縮性フィルムと比
較して、かなり高温にしなければ熱収縮を生しさせるこ
とか出来ず、しかも、熱収縮包装温度範囲か狭く、熱収
縮包装適性としてこよ、必ずしも良好とは言えない。
<Prior art> As heat-shrinkable films conventionally used in the field of heat-shrinkable packaging, there are various films made of polyethylene resin, polypropylene resin, polyvinyl chloride resin, etc. It is commercially available. Even inside,
Heat-shrinkable films made of polypropylene resin are widely used due to their inherent excellent properties such as transparency, gloss, moisture resistance, and non-polluting properties. However, compared to heat-shrinkable films made of polyvinyl chloride resin, etc., heat-shrinkable films made of polypropylene resin cannot be made to shrink unless heated to considerably higher temperatures, and the heat-shrinkable packaging temperature The range is narrow and suitability for heat shrink packaging is not necessarily good.

この様な欠点を解決する方法として、本発明者等はすて
に、両級外層がポリプロピレン系樹脂で芯層が特殊な直
鎖状低密度ポリエチレン樹脂を主体とする樹脂組成物を
積層させる方法等を見いだした。 (特願昭(i2−4
8444) シかし、上記方法に於いては、アンチブロ
ッキング剤や滑剤の添加量を通常の量にすると、滑り性
が不足し包装時の機微適性が低下してしまうと云う問題
が生した。そこで、良好なる滑り性を得ようとして、最
外層に多量の滑剤を添加すると、層間接着性が低下し、
溶断シール強度や物理的強度が弱くなった。又、最外層
に多量のアンチブロッキング剤を添加すると、今度は透
明性が悪くなるばかりか、ホットタック性も低下し溶断
シール性が悪くなってしまった。
As a method to solve these drawbacks, the present inventors have developed a method in which both outer layers are made of a polypropylene resin and the core layer is made of a special linear low-density polyethylene resin. etc. were found. (Tokugansho (i2-4
8444) However, in the above method, when the amount of anti-blocking agent or lubricant added is the normal amount, there is a problem that slipperiness is insufficient and sensitivity during packaging is reduced. Therefore, if a large amount of lubricant is added to the outermost layer in an attempt to obtain good lubricity, the interlayer adhesion will decrease.
The fusing seal strength and physical strength have become weaker. Moreover, when a large amount of anti-blocking agent was added to the outermost layer, not only the transparency deteriorated, but also the hot tack property deteriorated and the melt sealability deteriorated.

(本発明が解決しようとする問題点) 本発明は、低温での熱収縮性に優れ、熱収縮包装適性温
度範囲が広い、ポリプロピレン系樹脂を用いた多層熱収
縮性フィルムに於て、優れた滑り性を得ると共に、光学
特性や溶断シール性をも良好にしようとするものである
(Problems to be Solved by the Invention) The present invention provides an excellent multilayer heat-shrinkable film using polypropylene resin, which has excellent heat-shrinkability at low temperatures and a wide temperature range suitable for heat-shrink packaging. In addition to obtaining slipperiness, the objective is to improve optical properties and melt-cut sealing properties.

即ち、ポリプロピレン系樹脂が本来有している透明性や
光沢、更には、熱収縮包装用として重要な溶断シール性
等を阻害しな様に、滑剤やアンチブロッキング剤を通常
の添加量にしても、良好なる滑り性が得られる様なフィ
ルム構成を提供しようとするものである。
In other words, even if the lubricant and anti-blocking agent are added in the usual amount, so as not to interfere with the inherent transparency and gloss of polypropylene resin, as well as the fusing and sealing properties that are important for heat-shrinkable packaging. The purpose of this invention is to provide a film structure that provides good slipperiness.

(問題を解決するための手段) まず、本発明者等が以前に熱収縮包装適性に優れたフィ
ルムとして見いだした、両級外層がポリプロピレン系樹
脂て芯層が特殊な直鎖状低密度ポリエチレン樹脂からな
る積層熱収縮性フィルムに於いて、なぜ通常の滑剤添加
量で良好なる滑り性が得られないか色々検討した。その
結果、最外層のポリプロピレン系樹脂に添加された滑剤
が芯層の特殊な直鎖状低密度ポリエチレン樹脂に移行し
てしまい、表面にはブリートしにくいためである事が判
った。
(Means for Solving the Problem) First, the inventors of the present invention have previously discovered a film made of a polypropylene-based resin for both outer layers and a special linear low-density polyethylene resin for the core layer. Various studies were conducted to find out why good lubricity could not be obtained with the addition of a normal amount of lubricant in a laminated heat-shrinkable film made of . As a result, it was found that the lubricant added to the polypropylene resin in the outermost layer migrated to the special linear low-density polyethylene resin in the core layer, making it difficult to bleed onto the surface.

そこで、本発明では、最外層に添加された滑剤が芯層に
移行し難いようここ、最外層と芯層との間に遮蔽Nを設
けることにより問題解決を図った。
Therefore, in the present invention, the problem was solved by providing a shield N between the outermost layer and the core layer so that the lubricant added to the outermost layer does not easily migrate to the core layer.

即ち、低温での熱収縮性と熱収縮包装適性温度範囲に便
れ、しかも、良好なる滑り性と光学的特性、さらには、
優れた溶断シール性をも有した多層熱収縮性フィルムを
得るために、次のようなフィルム構成にするものである
。まず、両級外層が融点135〜150℃の結晶性ポリ
プロピしン系樹脂からなり、芯層が密度0.890〜0
.910 g /c++?で、ビカフト軟化点60〜8
0℃の直鎖状低密度ポリエチレン樹脂を主体とする樹脂
組成物からなり、しかも、両級外層と芯層との間の少な
くとも一方に、上記結晶性ポリプロピレン系樹脂と、同
じく上記直鎖状低密度ポリエチレン樹脂の中から選ばれ
た樹脂が、重量比で2:3〜3:1の範囲で混合され、
しかも、該結晶性ポリプロピレン系樹脂のメルトフロー
インデックス(以下Pvi Iと称す。)が、該直鎖状
低密度ポリエチレン樹脂のき41よりも高い樹脂組成物
からなる遮断層を挿入させ、更に、少なくとも一方の最
外層は勿論、該遮断層と芯層にも滑剤を添加させる。モ
して好ましくは、該遮断層の結晶性ポリプロピしン系樹
脂が、両級外層に使用されている結晶性ポリプロとレン
系樹脂と、又、同しく遮断層の直鎖状低回塵ポリエチレ
ン樹脂が、芯層に使用されている直鎖状低密度ポリエチ
レン樹脂と同一の樹脂を用いる。更;こ、該遮断層の各
厚みは、全体厚みの7〜30%であるのが好ましい。
That is, it has good heat shrinkability at low temperatures and a suitable temperature range for heat shrink packaging, and also has good slip properties and optical properties.
In order to obtain a multilayer heat-shrinkable film that also has excellent melt sealability, the following film structure is used. First, both outer layers are made of crystalline polypropylene resin with a melting point of 135 to 150°C, and the core layer has a density of 0.890 to 0.
.. 910 g/c++? So, Vikaft softening point is 60~8
It is made of a resin composition mainly composed of a linear low-density polyethylene resin at 0°C, and at least one of the outer layers and the core layer contains the above-mentioned crystalline polypropylene resin and the above-mentioned linear low-density polyethylene resin. Resins selected from density polyethylene resins are mixed in a weight ratio of 2:3 to 3:1,
Moreover, a barrier layer made of a resin composition in which the melt flow index (hereinafter referred to as Pvi I) of the crystalline polypropylene resin is higher than that of the linear low density polyethylene resin is inserted, and furthermore, at least A lubricant is added not only to one of the outermost layers but also to the barrier layer and the core layer. More preferably, the crystalline polypropylene resin of the barrier layer is the same as the crystalline polypropylene resin used in both outer layers, and the linear low dust polyethylene resin of the barrier layer. The same resin as the linear low density polyethylene resin used for the core layer is used. Furthermore, each thickness of the barrier layer is preferably 7 to 30% of the total thickness.

以下、本発明の構成を詳細に説明する。まず、本発明の
多層熱収縮性フィルムの基本的フィルム構成としては、
最外層/遮断N/芯N/遮断N/最外層、又;よ、最外
層/遮断N/芯層/最外層である。
Hereinafter, the configuration of the present invention will be explained in detail. First, the basic film structure of the multilayer heat-shrinkable film of the present invention is as follows:
Outermost layer/blocking N/core N/blocking N/outermost layer, or; yo, outermost layer/blocking N/core layer/outermost layer.

そして、両級外N:こ用いる結晶性ポリプロピレン系樹
脂としては、融点が135〜150℃の範囲のものであ
り、この様な結晶性ポリプロピレン系樹脂としては、プ
ロピレンにエチレンを2〜4−・t%程度共重合させた
ものや、プロピレンにエチレンとブテンとを3〜8−・
t%程度共重合させたものが好んで用いられる。
And, non-class N: The crystalline polypropylene resin to be used has a melting point in the range of 135 to 150°C. Copolymerization of about t% of ethylene and butene to propylene, 3 to 8-.
Copolymerization of approximately t% is preferably used.

次に、中間層に用いる直鎖状低密度ポリエチレン樹脂と
しては、エチレンとα−オレフィンとを共重合させ、直
鎖状の主鎖に短鎖分岐を導入させた樹脂である。尚、該
樹脂の短鎖分岐の数としては、従来の一般的な線状低密
度ポリエチレンの分岐の数よりも多数導入されており、
その事乙こより、密度を0.890〜0.910 g/
cm’と低く抑え、しかも、ヒカツト軟化点も60〜8
0℃と低くしている。尚、直鎖状低密度ポリエチレン樹
脂を主体とする樹脂組成物とは、該直鎖状低密度ポリエ
チレン樹脂単体は勿論、該直鎖状低密度ポリエチレン樹
脂に30wt%程度までのポリエチレン樹脂やポリプロ
ピレン樹脂、或は、エチレン−酢酸ビニル共重合体等の
ポリオレフィン系樹脂を1種、又は、2種以上を混合し
た樹脂組成物等を意味する。
Next, the linear low-density polyethylene resin used for the intermediate layer is a resin in which ethylene and α-olefin are copolymerized to introduce short chain branches into the linear main chain. In addition, the number of short chain branches of this resin is greater than the number of branches of conventional general linear low density polyethylene,
Therefore, the density should be set at 0.890 to 0.910 g/
cm' and low softening point of 60 to 8.
The temperature is kept as low as 0℃. Note that a resin composition mainly composed of a linear low-density polyethylene resin refers to not only the linear low-density polyethylene resin itself, but also the linear low-density polyethylene resin containing up to about 30 wt% of polyethylene resin or polypropylene resin. , or a resin composition containing one or more polyolefin resins such as ethylene-vinyl acetate copolymer.

更に、両級外層と芯層との間の少なくとも一方に挿入さ
れる遮断層に用いる結晶性ポリプロピレン系樹脂として
は、両級外層に使用出来る結晶性ポリプロピレン系樹脂
の中から選ばれた樹脂が用いられる。しかし、下記する
直鎖状低密度ポリエチレン樹脂のMlよりも高いMIを
有する結晶性ポリプロピレン系樹脂でなくてはならない
。尚、該結晶性ポリプロピレン系樹脂として、両級外層
に用いられている結晶性ポリプロピレン系樹脂と同一の
樹脂を用いることが、熱収縮性や生産性の面から好まし
い。
Furthermore, as the crystalline polypropylene resin used for the barrier layer inserted between at least one of the outer layer and the core layer, a resin selected from among the crystalline polypropylene resins that can be used for the outer layer of both grades is used. It will be done. However, the crystalline polypropylene resin must have a higher MI than the linear low density polyethylene resin described below. Note that it is preferable to use the same crystalline polypropylene resin used for both outer layers as the crystalline polypropylene resin in terms of heat shrinkability and productivity.

叉、該遮断層に用いる直鎖状低密度ポリエチレン樹脂と
しては、芯層に使用出来ろ直鎖状低密度ポリエチレン樹
脂の中から選ばれた樹脂が用いられる。しかし、上記し
た如く、該直鎖状低密度ポリエチレン樹脂は、上記結晶
性ポリプロピレン系樹脂のMlよりも低いMlを有する
ものでなくてはならない。尚、該直鎖状低密度ポリエチ
レン樹脂として、芯層に用いられている直鎖状低密度ポ
リエチレン樹脂と同じ樹脂を用いることが、熱収縮性や
生産性の面から好ましい。
As the linear low-density polyethylene resin used for the barrier layer, a resin selected from linear low-density polyethylene resins that can be used for the core layer is used. However, as mentioned above, the linear low density polyethylene resin must have a lower Ml than the Ml of the crystalline polypropylene resin. In addition, it is preferable to use the same resin as the linear low-density polyethylene resin used for the core layer as the linear low-density polyethylene resin in terms of heat shrinkability and productivity.

尚、本発明に於けるMIは、結晶性ポリプロピレン系樹
脂も直鎖状低密度ポリエチレン樹脂も共にJ I S 
 K−72!OのA法に準じて、温度230℃。
Incidentally, MI in the present invention is JIS for both crystalline polypropylene resin and linear low density polyethylene resin.
K-72! Temperature 230°C according to Method A of O.

荷重2160gの同一条件で測定された値である。This is a value measured under the same conditions with a load of 2160 g.

これら各樹脂と本発明との関係について更に詳しく説明
すると、まず、両級外層に用いる結晶性ポリプロピレン
系樹脂の融点が150℃を越えると、低温での延伸加工
が困難になるため、高温で延伸加工される様になるので
、低温での熱収縮性が低下するのは勿論、高温での熱収
縮性も懇くなり、熱収縮包装適性が低下してしまうこと
;こなる。叉、上記融点が、135℃未満であると、耐
熱性に劣り、収縮トンネル内で溶融白化等を生しやすく
なり、やはり熱収縮包装適性が低下してしまう。
To explain in more detail the relationship between each of these resins and the present invention, firstly, if the melting point of the crystalline polypropylene resin used for both class outer layers exceeds 150°C, it will be difficult to stretch at low temperatures. As the material is processed, its heat-shrinkability at low temperatures not only decreases, but also its heat-shrinkability at high temperatures deteriorates, reducing its suitability for heat-shrinkable packaging. On the other hand, if the melting point is less than 135°C, the heat resistance will be poor and melt whitening will easily occur in the shrink tunnel, resulting in a decrease in suitability for heat shrink packaging.

次に、芯層に用いる直鎖状低密度ポリエチレン樹脂の密
度が0.910 g /(−I11’を越えると、延伸
性が低下し、特に、低温での延伸が不可能になってしま
い、その結果、低温での熱収縮性が劣り、熱収縮包装適
性温度範囲が狭くなってしまう。又、上記密度が0.8
90 g/ cm’未満であると、得られる多層熱収縮
性フィルムの自然収縮性を無くするための熱処理が困難
となりフィルムが変形したり、平滑性か悪化したりして
しまう。更に、直鎖状低密度ポリエチレンのビカット軟
化点が80°Cを越えろと、低温での延伸加工が困難に
なり、高温で延伸加工する様になるので、低温での熱収
縮性が向上せず、熱収縮包装適性温度範囲を広げること
が出来ない。
Next, when the density of the linear low-density polyethylene resin used for the core layer exceeds 0.910 g/(-I11', the stretchability decreases, and in particular, stretching at low temperatures becomes impossible. As a result, the heat shrinkability at low temperatures is poor, and the suitable temperature range for heat shrink packaging becomes narrow.Also, the above density is 0.8
If it is less than 90 g/cm', it will be difficult to perform heat treatment to eliminate natural shrinkage of the resulting multilayer heat-shrinkable film, resulting in deformation of the film or deterioration of its smoothness. Furthermore, if the Vicat softening point of linear low-density polyethylene exceeds 80°C, it will become difficult to stretch at low temperatures, and it will be necessary to stretch at high temperatures, so the heat shrinkability at low temperatures will not improve. , it is not possible to widen the suitable temperature range for heat shrink packaging.

又、上記ビカット軟化点が60℃未満であると、両級外
層の結晶性ポリプロピレン系樹脂が延伸加工される最適
温度範囲では温度が高すぎて、延沖効果が充分発揮され
ず、熱収縮包装適性の向上に繋がらない。
In addition, if the Vicat softening point is less than 60°C, the temperature will be too high in the optimum temperature range in which the crystalline polypropylene resin of both class outer layers is stretched, and the Nobeoki effect will not be fully exhibited, resulting in heat shrink packaging. It does not lead to improvement in aptitude.

又、これらの直鎮状低密度ポリエチレン樹脂に前記した
他のポリオレフィン系樹脂が3kt9≦を越えて混入さ
れると、該直鎖状低密度ポリエチレン樹脂の有している
延伸加工のしやすさや、熱収縮性フィルムとしての優れ
た熱収縮特性を具備させることが出来なくなってしまう
In addition, when other polyolefin resins mentioned above are mixed into these straight-chain low-density polyethylene resins in an amount exceeding 3kt9≦, the ease of stretching process that the straight-chain low-density polyethylene resins have, It becomes impossible to provide excellent heat shrinkage properties as a heat shrinkable film.

更に、本発明の重要な特長である、最外層と芯層との間
で滑剤の移行を阻止する遮断層に用いる結晶性ポリプロ
ピレン系樹脂と直鎖状低密度ポリエチレン樹脂について
説明する。まず、これらの樹脂は雨量外層や芯層に使用
できる樹脂てないと本発明の特長である熱収縮性を発揮
させることが出来ない。そして、結晶性ポリプロピレン
系樹脂のMIが、直鎖状低密度ポリエチレン樹脂のM 
1よりも低いと、相溶性が悪く、溶融押出時の地合が低
下し、得られる多層熱収縮性フィルムの透明性が悪くな
ってしまう。尚、一般にはポリプロピレン樹脂とポリエ
チレン樹脂とを混合する場合、片方が少量であれはさほ
ど地合は悪くならず透明性を低下させないが、本発明の
様な組成割合では、上記の如きMIのものてないと相溶
性が不十分て地合が悪くなり透明性を低下させてしまう
Furthermore, the crystalline polypropylene resin and linear low-density polyethylene resin used in the barrier layer that prevents the transfer of lubricant between the outermost layer and the core layer, which are important features of the present invention, will be explained. First of all, these resins cannot exhibit the heat shrinkability that is a feature of the present invention unless they can be used for the outer rain layer and the core layer. The MI of the crystalline polypropylene resin is the M of the linear low density polyethylene resin.
If it is lower than 1, the compatibility will be poor, the formation during melt extrusion will be poor, and the transparency of the resulting multilayer heat-shrinkable film will be poor. Generally, when polypropylene resin and polyethylene resin are mixed, if a small amount of one of the resins is used, the formation will not deteriorate so much and the transparency will not be reduced. If not, the compatibility will be insufficient, resulting in poor formation and reduced transparency.

又、結晶性ポリプロピレン系樹脂と直鎖状低密度ポリエ
チレン樹脂との組成割合か2:3〜3:1の範囲を外れ
ると、滑剤の遮蔽層としての働きが悪くなり本発明の特
長が無くなってしまう。その理由は明らかではないが、
結晶性ポリプロピレン系樹脂の組成割合が上記条件を越
えると遮断層の滑剤が芯層に移行し易くなり、遮断効果
が低下するものと思われる。尚、この場合最外層の滑剤
は、遮断層の結晶性ポリプロピレン系樹脂成分か多いた
め、遮断層には容易に移行するものと思われる。
Furthermore, if the composition ratio of crystalline polypropylene resin and linear low density polyethylene resin is outside the range of 2:3 to 3:1, the lubricant will not function as a shielding layer and the features of the present invention will be lost. Put it away. The reason is not clear, but
It is believed that if the composition ratio of the crystalline polypropylene resin exceeds the above conditions, the lubricant in the barrier layer tends to migrate to the core layer, reducing the barrier effect. In this case, the lubricant in the outermost layer is considered to be easily transferred to the barrier layer since it is mostly a crystalline polypropylene resin component of the barrier layer.

又、直鎖状低密度ポリエチレン樹脂が上記条件を越える
と、最外層の滑剤が遮断層に移行し易くなり遮断効果が
無くなるものと思われる。尚、この場合にも遮断層の滑
剤は、芯層の直鎖状低密度ポリエチレン樹脂成分が多い
ため、容易に移行するものと思われる6即ち、最外層や
芯層の樹脂と遮断層に使用される大部分の樹脂とが同一
樹脂である場合には、それぞれの眉間で滑剤は移行しや
すいものと思われる。しかも、遮断層の結晶性ポリプロ
ピレン系樹脂の割合が大きくなり過ぎると、遮断層に移
行してきた滑剤が芯層に引き寄せられやすく、又、遮断
層の直鎖状低密度ポリエチレン樹脂の割合が大きくなり
過ぎると、最外層の結晶性ポリプロピレン系樹脂層に添
加された滑剤が遮断層に引き寄せられやすくなるものと
思われる。
Furthermore, if the linear low-density polyethylene resin exceeds the above conditions, the lubricant in the outermost layer tends to migrate to the barrier layer, and the barrier effect is likely to be lost. In this case as well, the lubricant in the barrier layer is likely to transfer easily because the core layer contains a large amount of linear low-density polyethylene resin. If most of the resin used is the same resin, it is thought that the lubricant will easily transfer between the eyebrows. Moreover, if the ratio of crystalline polypropylene resin in the barrier layer becomes too large, the lubricant that has migrated to the barrier layer will be easily attracted to the core layer, and the ratio of linear low-density polyethylene resin in the barrier layer will increase. If it is too long, it is thought that the lubricant added to the outermost crystalline polypropylene resin layer is likely to be attracted to the barrier layer.

尚、この様な遮断層は、片方の最外層にのみ良好なる滑
り性が必要な場合には、該最外層と芯層との間にのみ設
けてもよいが、一般には雨量外層と芯層との両方の間に
設けるのか好ましい。更に、雨量外層と芯層との間にこ
の様な遮断層を設けることは、層間接着強度をより増強
させることになり、溶断シール強度や物理強度の向上に
も繋がる。
In addition, such a barrier layer may be provided only between the outermost layer and the core layer if good slipperiness is required for only one outermost layer, but generally, the barrier layer is provided between the outermost layer and the core layer. It is preferable to provide it between both. Furthermore, providing such a barrier layer between the outer rain layer and the core layer further increases the interlayer adhesive strength, which also leads to improvements in the fusing seal strength and physical strength.

遮断層や芯層に添加する滑剤としては、従来−般に使用
されているアマイド系の滑剤が使用出来る。そして、遮
断層には1000〜3000ppm程度、芯層には20
00〜4000ppm程度添加するのが好ましい。尚、
添加量が多くなり過ぎると今度は層間接着強度か低下し
て好ましくない。又、最外層には滑り性を必要とする側
の層にのみ、遮断層や芯層に用いたと同じ様な滑剤を1
000〜2000ppm程度添加すればよいが、一般に
は雨量外層に添加する。尚、滑り性を必要とする最外層
には、一般のシリカ系アンチブロッキング剤も500〜
2000ppm程度添加するのか好ましい。
As the lubricant to be added to the barrier layer and the core layer, amide-based lubricants that are commonly used in the past can be used. The barrier layer contains about 1,000 to 3,000 ppm, and the core layer contains about 20 ppm.
It is preferable to add about 00 to 4000 ppm. still,
If the amount added is too large, the interlayer adhesive strength will decrease, which is not preferable. In addition, one layer of the same lubricant used for the barrier layer and core layer is added only to the outermost layer that requires slipperiness.
It may be added in an amount of about 000 to 2000 ppm, but it is generally added to the outer layer of rainfall. In addition, for the outermost layer that requires slipperiness, a general silica-based anti-blocking agent can also be used.
It is preferable to add about 2000 ppm.

本発明の多層熱収縮性フィルムの全体厚みは、その用途
から10・〜30μの範囲内であることが好ましい。そ
して、遮断層の厚みについては、前記した如く該層の厚
み割合が全体厚みの7〜30%の範囲内であることか遮
断効果と熱収縮特性の面から好ましい。更に、芯層の厚
みは全体厚みの25〜70%の範囲内である事か熱収縮
包装適性温度範囲の面から好ましい。
The overall thickness of the multilayer heat-shrinkable film of the present invention is preferably within the range of 10 to 30 μm in view of its intended use. As for the thickness of the barrier layer, it is preferable from the viewpoint of barrier effect and heat shrinkage properties that the thickness ratio of the layer is within the range of 7 to 30% of the total thickness as described above. Furthermore, it is preferable that the thickness of the core layer be within the range of 25 to 70% of the total thickness, in view of the suitable temperature range for heat shrink packaging.

尚、本発明の要旨を変更しない範囲内で、各層に池の樹
脂や各種添加剤を混入したり、或は、新たな層を設けた
りする事は何等妨げられるものではない。
It should be noted that, within the scope of not changing the gist of the present invention, there is no hindrance to mixing resin or various additives into each layer or providing a new layer.

次に、本発明の多層熱収縮性フィルムを製造する方法は
、特に限定されるものではないが、次の様な方法により
製造されるのが好ましい。即ち、複数の押出機を用い多
層ダイより多1来延伸原反シートを共押出する。そして
、該多層未延伸原反シートを冷却固化させた後、延伸可
能な温度まで再加熱して、縦方向、横方向共に少なくと
も3.0倍以上延伸する。延伸方法としては、テンタ一
方式、或は、インフし−ション方式共可能であるが、縦
方向と横方向の熱収縮特性をよく近似させるのが容易で
あることから、インフレーション方式により製造するの
が好ましい。そのために、多層未延伸原反シートは多層
サーキュラ−ダイを用い、多層チューブ状シートとして
得ることが必要である。
Next, the method for producing the multilayer heat-shrinkable film of the present invention is not particularly limited, but it is preferably produced by the following method. That is, a plurality of stretched raw sheets are coextruded from a multilayer die using a plurality of extruders. After the multilayer unstretched raw sheet is cooled and solidified, it is reheated to a temperature at which it can be stretched, and stretched by at least 3.0 times in both the longitudinal and transverse directions. As for the stretching method, both the tenter type and the inflation method are possible, but since it is easy to closely approximate the heat shrinkage characteristics in the longitudinal and transverse directions, it is preferable to use the inflation method. is preferred. For this purpose, it is necessary to use a multilayer circular die to obtain the multilayer unstretched raw sheet as a multilayer tubular sheet.

そして、得られた多層二軸延伸フィルムは、自然放置し
ていると該フィルム自体の持っている自然収縮性によっ
て変形や表面状態が悪化するので、これを防止するため
に熱収縮特性を余り低下させない様に熱処理して、自然
収縮量を減らすことがより好ましい。
If the obtained multilayer biaxially stretched film is left to naturally shrink, deformation and surface condition will deteriorate due to the natural shrinkage of the film itself, so in order to prevent this, the heat shrinkage characteristics are not reduced too much. It is more preferable to perform heat treatment to reduce the amount of natural shrinkage.

本発明の多層熱収縮性フィルムを用いた熱収縮包装方法
としては、従来のポリプロピレン樹脂よりなる熱収縮性
フィルムに用いられている熱収縮包装ラインをそのまま
使用することが出来る。しかも、本発明の多層熱収縮性
フィルムは滑り性に優れているので包装時の機械適性が
良好であり、容易に包装することが出来るばかりか、収
縮トンネル内の温度をシビャーに設定しなくても容易に
良好なる熱収縮包装体を得ろことが出来る。
As a heat-shrink packaging method using the multilayer heat-shrinkable film of the present invention, a heat-shrink packaging line used for conventional heat-shrinkable films made of polypropylene resin can be used as is. In addition, the multilayer heat-shrinkable film of the present invention has excellent slip properties, so it has good mechanical suitability during packaging, and not only can it be easily packaged, but the temperature inside the shrink tunnel does not have to be set severely. It is also possible to easily obtain a good heat-shrinkable package.

(発明の効果〉 続いて本発明の詳細な説明すると、まず、本発明の多層
熱収縮性フィルムは、芯層の直鎖状低密度ポリエチレン
樹脂が低温熱収縮性に優れているので、低温より熱収縮
を開始させることが出来る。
(Effects of the Invention) Next, the present invention will be explained in detail. First, the multilayer heat-shrinkable film of the present invention has excellent low-temperature heat-shrinkability because the linear low-density polyethylene resin of the core layer has excellent low-temperature heat-shrinkability. Heat shrinkage can be initiated.

しかも、菌叢外層の結晶性ポリプロピレン系樹脂が耐熱
性を有しているので、高温でも溶融白化等を生じる様な
こともなく、良好なる熱収縮包装体が得られる。即ち、
この様なフィルム構成にすることにより、熱収縮包装適
性温度範囲を広くする事が出来る。しかも、菌叢外層に
使用される樹脂が、延伸加工性に優れているばかりか、
芯層に使用される樹脂も低温での延伸性が良好であるた
めに、低温で容易に延伸する事が出来、低温収縮性を向
上させることが出来る。更に、最外層と芯層との間に滑
剤の移行を阻止する遮断層を設けた事により、最外、1
の滑剤が芯層に移行せず、表面にブリードする様になる
ので、少量の滑剤添加量でも良好なる滑り性が得られる
。又、遮断層に用いられる樹脂同士は相溶性に優れてい
るので透明性も良好であり、デイスプレー効果に優れた
熱収縮包装体が得られる。その上、滑剤の添加量を少な
くすることや、最外層と芯層の両方に良好なる接着性を
有する遮断層を設けることにより、より一層層間接着性
が増し、溶断シール強度や物理強度が向上する。又、ア
ンチブロッキング剤の添加量も少なくてすむので、透明
性が良好に成るばかりか、ホットタック性も向上するの
て溶断シール時のシール不良も無くなる。
Moreover, since the crystalline polypropylene resin of the outer layer of bacterial flora has heat resistance, a good heat-shrinkable package can be obtained without melting and whitening even at high temperatures. That is,
By adopting such a film configuration, the suitable temperature range for heat shrink packaging can be widened. Moreover, the resin used for the outer layer of bacterial flora not only has excellent stretchability, but also
Since the resin used for the core layer also has good stretchability at low temperatures, it can be easily stretched at low temperatures and the low-temperature shrinkability can be improved. Furthermore, by providing a barrier layer between the outermost layer and the core layer to prevent the transfer of lubricant, the outermost
Since the lubricant does not migrate to the core layer and bleeds to the surface, good lubricity can be obtained even with a small amount of lubricant added. Furthermore, since the resins used in the barrier layer have excellent compatibility with each other, transparency is also good, and a heat-shrinkable package with excellent display effects can be obtained. In addition, by reducing the amount of lubricant added and providing a barrier layer with good adhesion to both the outermost layer and the core layer, interlayer adhesion is further increased, improving fusion seal strength and physical strength. do. In addition, since the amount of anti-blocking agent added is small, not only transparency is improved, but also hot tack properties are improved, eliminating sealing defects during fusing sealing.

(実施例) 以下に実施例、及び、比較例を示し、本発明を具体的に
説明する。
(Example) The present invention will be specifically explained by showing Examples and Comparative Examples below.

実施例1 融点138℃の結晶性ポリプロピレン系樹脂を菌叢外層
とし、密度0.900 g、 / CM?、ビカット軟
化点70℃の直鎖状低密度ポリエチレン樹脂を芯、1と
し、更に、菌叢外層に用いた結晶性ポリプロピレン系樹
脂と芯層に用いた直鎖状低密度ポリエチレン樹脂を重量
比で1:l:こ混合した樹脂組成物を遮断層とする、最
外層/遮断N/芯層/遮断N/最外層の構成を有するチ
ューブ状共押出多層未延伸原反シートを3台の押出機と
3種5Nの共押出用サーキュラ−ダイによって得た。押
出成形に際しては、共押出直後に水冷方式によって急冷
させた。尚、該実施例1に用いた結晶性ポリプロピレン
系樹脂と直鎖状低密度ポリエチレン樹脂のN冒はそれぞ
れ、3.2g/minと1.8g/minであった。そ
し・で、菌叢外層:ここよ滑剤を1500ppmとアン
チブロッキング剤を1500ppm添加し、芯層と遮断
層には菌叢外層と同じ滑剤をそれぞれ3000ppmと
2000ppm添加した。
Example 1 A crystalline polypropylene resin with a melting point of 138°C was used as the bacterial flora outer layer, and the density was 0.900 g/CM? A linear low-density polyethylene resin with a Vicat softening point of 70°C was used as the core 1, and a weight ratio of the crystalline polypropylene resin used for the bacterial flora outer layer and the linear low-density polyethylene resin used for the core layer was added. 1:l: A tubular coextruded multilayer unstretched raw sheet having a structure of outermost layer/blocking N/core layer/blocking N/outermost layer with the mixed resin composition as a blocking layer is extruded using three extruders. and three types of 5N were obtained using a circular die for coextrusion. During extrusion molding, the coextrusion was immediately followed by rapid cooling using a water cooling method. Note that the N flux of the crystalline polypropylene resin and the linear low density polyethylene resin used in Example 1 was 3.2 g/min and 1.8 g/min, respectively. Then, to the bacterial flora outer layer: 1500 ppm of a lubricant and 1500 ppm of an anti-blocking agent were added here, and the same lubricant as the bacterial flora outer layer was added to the core layer and barrier layer at 3000 ppm and 2000 ppm, respectively.

又、得られた多層未延伸原反シートの全体厚みは240
μで、各層の厚み比は一方の最外層からに〇。
In addition, the total thickness of the obtained multilayer unstretched raw sheet was 240
μ, and the thickness ratio of each layer is from one outermost layer to 〇.

5:2: 0.5: 1てあった。It was 5:2:0.5:1.

この多層未延伸原反シートを、従来のインフレーション
方式によって縦方向、横方向共に4.2倍に延伸したが
、従来のポリプロピレン系熱収縮性フィルムよりも低温
で容易に延伸加工出来、多層二軸延伸フィルムを得るこ
とが出来た。そして、この二軸延伸フィルムに弛緩を与
えながら熱固定を行ない、全体厚みが約15μの多層熱
収縮性フィルムを得た。
This multilayer unstretched raw sheet was stretched 4.2 times in both the longitudinal and transverse directions using a conventional inflation method. A stretched film could be obtained. Then, this biaxially stretched film was heat-set while being relaxed to obtain a multilayer heat-shrinkable film having a total thickness of about 15 μm.

得られた多層熱収縮性フィルムを用いてノート・ブック
2冊の集積熱収縮包装を行なった。その結果、何等トラ
ブルも無く容易に包装機械に掛けることが出来、しかも
、160℃に設定された収縮トンネル温度を上下に15
゛C程度変化させても、緊迫性に劣ったり、コーナ一部
に皺を生したりする様なこともなく、その上、溶融白化
したりする様なこともなく、良好なる仕上がりが得られ
た。又、溶断シール時にホットタック性の悪さ:こよろ
シール不良を生じる様なこともなく、しかも、得られた
熱収縮包装体の溶断シール強度は強く、包装体を折り曲
げても溶断シール部より破袋する様なこともなかった。
Using the obtained multilayer heat-shrinkable film, two notebooks were integrated into heat-shrinkable packaging. As a result, it can be easily placed on the packaging machine without any trouble, and the shrink tunnel temperature set at 160℃ can be raised or lowered by 15 degrees.
Even if the material is changed by ゛C, a good finish can be obtained without poor tightness or wrinkles in some corners, and also without melting and whitening. Ta. In addition, there is no poor hot tack property when sealing by fusing: there is no occurrence of a defective seal, and the strength of the fusing seal of the resulting heat-shrinkable package is strong, and even if the package is folded, it will not break from the fusing seal. There was no need to bag it.

(比較例1〜2) 雨量外層を比較例1ては融点154℃の、比較例2ては
融点132℃の結晶性ポリプロピレン系樹脂とし、芯層
及び遮断層には実施例1と同し樹脂を用い、しかも、各
層の厚み構成や全体厚み、更には、各層の添加剤の種類
と添加量等に間しても実施例1と同じ多層未延伸原反シ
ートを、実施例1と同様の方法によって共押出した。
(Comparative Examples 1 to 2) The outer layer of rainfall was made of a crystalline polypropylene resin with a melting point of 154°C in Comparative Example 1 and 132°C with a melting point in Comparative Example 2, and the same resin as in Example 1 was used for the core layer and barrier layer. In addition, a multilayer unstretched raw sheet was prepared in the same manner as in Example 1, and the thickness structure and overall thickness of each layer, as well as the type and amount of additives in each layer, were the same as in Example 1. Coextruded by method.

得られた多層未延伸原反シートを、実施例1と同様、従
来のインフレーション方式によって二軸延伸を行なった
。その結果、比較例1ては実施例1よりも高温でないと
延伸出来なかった。しかし、比較例2ては、低温でも延
伸することが出来た。
The obtained multilayer unstretched raw sheet was biaxially stretched in the same manner as in Example 1 using the conventional inflation method. As a result, Comparative Example 1 could not be stretched at a higher temperature than Example 1. However, in Comparative Example 2, stretching was possible even at low temperatures.

そして、これら二軸延伸フィルムに実施例1と同様に熱
固定を行なって多層熱収縮性フィルムを得た。
Then, these biaxially stretched films were heat-set in the same manner as in Example 1 to obtain a multilayer heat-shrinkable film.

得られた多層熱収縮性フィルムを用いて、窓11きの箱
(通称ウィンドボックス)の熱収縮包装を行なった。そ
の結果、比較例1ては収縮トンネル温度が低い時は勿論
、高温時でも熱収縮性に劣り、コーナ一部等に皺が生じ
、良好なる熱収縮包装体が得られなかった。又、比較例
2では低温での熱収縮性は良好であったが、耐熱性に劣
り、収縮トンネル温度が少しても高くなるとウィンドボ
ックスの窓の部分で溶融白化を生じ、熱収縮包装適性温
度範囲としては狭くなり、良好なる熱収縮包装体が得ら
れ難かった。
Using the obtained multilayer heat-shrinkable film, a box with 11 windows (commonly known as a wind box) was heat-shrink wrapped. As a result, in Comparative Example 1, the heat shrinkability was poor not only when the shrink tunnel temperature was low, but also at high temperatures, and wrinkles were formed in some corners, so that a good heat shrink package could not be obtained. In addition, in Comparative Example 2, the heat shrinkability at low temperatures was good, but the heat resistance was poor, and if the shrink tunnel temperature rose even a little, melting and whitening occurred at the window part of the wind box, and the temperature suitable for heat shrink packaging was lowered. The range was narrow, and it was difficult to obtain a good heat-shrinkable package.

(比較例3) 雨量外層を実施例1と同じ結晶性ポリプロピレン系樹脂
とし、芯層を密度0.919 g /c−m’、ビカッ
ト軟化点90℃の一般的な線状低密度ポリエチレン樹脂
とし、遮断層には実施例1と同じ樹脂組成を用い、しか
も、各層の厚み構成や全体厚み、更には、各層の添加剤
の種類と添加量等に間しても実施例1と同じ多層未延伸
原反シートを、実施例1と同様の方法によって共押出し
た。
(Comparative Example 3) The outer rain layer was made of the same crystalline polypropylene resin as in Example 1, and the core layer was made of a general linear low-density polyethylene resin with a density of 0.919 g/cm' and a Vicat softening point of 90°C. The same resin composition as in Example 1 was used for the barrier layer, and the thickness structure and overall thickness of each layer, as well as the type and amount of additives in each layer, were the same as in Example 1. The stretched raw sheet was coextruded in the same manner as in Example 1.

得られた多層未延伸原反シートを、実施例1と同様、従
来のインフレーション方式によって二軸延伸を試みた。
As in Example 1, the obtained multilayer unstretched raw sheet was subjected to biaxial stretching using the conventional inflation method.

しかし、延伸開始点の温度を芯層の線状低密度ポリエチ
レン樹脂の融点に近い温度までも昇温しないと延伸出来
ず、しかも、延伸安定性に劣っていた。
However, stretching cannot be performed unless the temperature at the starting point of stretching is raised to a temperature close to the melting point of the linear low-density polyethylene resin of the core layer, and the stretching stability is poor.

(比較例4〜5) 雨量外層、芯層、及び、遮断層共に、実施例1と同し樹
脂を用い、遮断層の結晶性ポリプロピレン系樹脂と直鎖
状低密度ポリエチレン樹脂との混合割合のみを重量比で
比較例4てはl:2とし、比較例5ては4:1とし、し
かも、各層の厚み構成や全体厚み、更には、各層の添加
剤の種類と添加量等に関しては実施例1と同じ多層未延
伸原反シートを、実施例1と同様の方法によって共押出
した。
(Comparative Examples 4 to 5) The same resin as in Example 1 was used for both the rain layer, the core layer, and the barrier layer, and only the mixing ratio of the crystalline polypropylene resin and the linear low-density polyethylene resin of the barrier layer was used. The weight ratio was 1:2 in Comparative Example 4 and 4:1 in Comparative Example 5, and the thickness structure of each layer, the overall thickness, and the type and amount of additives in each layer were determined. The same multilayer unstretched raw sheet as in Example 1 was coextruded by the same method as in Example 1.

得られた多層未延伸原シートは、実施例1と同様、両者
共に容易に二軸延伸や熱固定を行なうことが出来、多層
熱収縮性フィルムを得ることが出来た。しかし、得られ
た多層熱収縮性フィルムは共に滑り性が悪く、包装機械
に掛かりにくいものてあった。
As in Example 1, the obtained multilayer unstretched original sheets could be easily biaxially stretched and heat-set, and a multilayer heat-shrinkable film could be obtained. However, the resulting multilayer heat-shrinkable films had poor slip properties and were difficult to hang on packaging machines.

比較例6 両最外層と芯層には実施例1と同1ノ樹脂を用い、遮断
層を融点137°CてM 11.2 g/ minの結
晶性ポリプロピレン系樹脂と、密度0.900 E /
c−m’、ヒカット軟化点67℃でM14.2g/m団
の直鎖状低密度ポリエチレン樹脂を重量比で1:1に混
合した樹脂組成とし、しかも、各層の厚み構成や全体厚
み、更には、各層の添加剤の種類と添加量等に関しては
実施例1と同し多層未延伸原反シートを、実施例1と同
様の方法によって共押出し・た。
Comparative Example 6 The same resin as in Example 1 was used for both outermost layers and the core layer, and the barrier layer was made of a crystalline polypropylene resin with a melting point of 137°C and a M of 11.2 g/min, and a density of 0.900 E. /
cm', Hikat softening point of 67°C, M14.2 g/m group linear low density polyethylene resin mixed in a weight ratio of 1:1, and the thickness structure of each layer, overall thickness, and A multilayer unstretched raw sheet was coextruded in the same manner as in Example 1, with the same types and amounts of additives in each layer as in Example 1.

得られた多層未延伸原シートは、実施例1と同様、容易
に二軸延伸や熱固定を行なうことが出来、多層熱収縮性
フィルムを得ることが出来た。しかし、得られた多層熱
収縮性フィルムは地合か悪く透明性に劣り、熱収縮包装
用としてはデイスプレー効果;こ劣るものであった。
The obtained multilayer unstretched original sheet could be easily biaxially stretched and heat-set as in Example 1, and a multilayer heat-shrinkable film could be obtained. However, the resulting multilayer heat-shrinkable film had poor texture and poor transparency, and its display effect was poor when used for heat-shrink packaging.

(比較例7) 各層に添加する滑剤とアンチブロッキング剤の添加量以
外は、実施例1と同し多層熱収縮性フィルムを実施例1
と同し方法によって得た。即ち、両最外層に滑剤を50
00ppm、アンチブロッキング剤を1500ppm添
加し、芯層と遮断層には滑剤を添加しなかった。
(Comparative Example 7) A multilayer heat-shrinkable film was prepared in the same manner as in Example 1 except for the amount of lubricant and anti-blocking agent added to each layer.
obtained by the same method. That is, 50% of lubricant was added to both outermost layers.
00 ppm, an anti-blocking agent was added at 1500 ppm, and no lubricant was added to the core layer and the barrier layer.

しかし、得られた多層熱収縮性フィルムは、最外層に多
量の滑剤を添加しているにもかかわらず、その表面は滑
り性が悪く、包装機械に掛かりにくいものであった。
However, despite the addition of a large amount of lubricant to the outermost layer of the obtained multilayer heat-shrinkable film, its surface had poor slipperiness and was difficult to hang onto packaging machines.

(比較例8) 両最外層と芯層に実施例1と同じ樹脂を用い、遮断1層
は設けられていない2種3層の多層熱収縮性フィルムを
、押出機の数と多層サーキュラ−ダイの種類を変える以
外は実施例1と同様な方法によって得た。尚、各層の厚
み比は1:3:lて、フィルム厚みは実施例1と同様的
15μであった。そして、両最外層には滑剤を3000
ppm、アンチブロッキング剤を3000pp111添
加し、芯層には滑剤を5000ppm添加させた。
(Comparative Example 8) The same resin as in Example 1 was used for both outermost layers and the core layer, and a 2-type, 3-layer multilayer heat-shrinkable film with no barrier layer was prepared by changing the number of extruders and the multilayer circular die. It was obtained in the same manner as in Example 1 except for changing the type of. The thickness ratio of each layer was 1:3:1, and the film thickness was 15 μm, which is the same as in Example 1. Then, apply 3000 lubricant to both outermost layers.
3,000 ppm of an anti-blocking agent was added, and 5,000 ppm of a lubricant was added to the core layer.

しかし、得られた多層熱収縮性フィルムは、各層に多量
の滑剤等を添加させているにもかかわらず、さほど滑り
性が向上しておらず、シv)も、層間接着強度が低下し
、溶断シール強度が弱くなっていた。又、アンチブロッ
キング剤を多量に添加しているため、ホットタック性が
低下し、溶断シール時にシール不良を生じやすかった。
However, despite the addition of a large amount of lubricant to each layer, the obtained multilayer heat-shrinkable film did not have much improved slipperiness, and in iv), the interlayer adhesive strength decreased, The strength of the fused seal was weakened. Furthermore, since a large amount of anti-blocking agent was added, hot tack properties were reduced, and sealing failures were likely to occur during fusing sealing.

Claims (1)

【特許請求の範囲】 1)両最外層が融点135〜150℃の結晶性ポリプロ
ピレン系樹脂からなり、芯層が密度0.890〜0.9
10g/cm^3で、ビカット軟化点60〜80℃の直
鎖状低密度ポリエチレン樹脂を主体とする樹脂組成物か
らなり、しかも、両最外層と芯層との間の少なくとも一
方に、上記結晶性ポリプロピレン系樹脂と上記直鎖状低
密度ポリエチレン樹脂の中から選ばれたそれぞれの樹脂
が重量比で2:3〜3:1の範囲で混合され、その上、
該結晶性ポリプロピレン系樹脂のメルトフローインデッ
クスが該直鎖状低密度ポリエチレン樹脂のメルトフロー
インデックスよりも高い樹脂組成物からなる遮断層が挿
入され、更に、少なくとも一方の最外層は勿論、該遮断
層と芯層にも滑剤が添加されている多層熱収縮性フィル
ム。 2)特許請求の範囲第1項記載の両最外層と芯層との間
の少なくとも一方に挿入される層の結晶性ポリプロピレ
ン系樹脂が、両最外層に使用されている樹脂と同一であ
る、多層熱収縮性フィルム。 3)特許請求の範囲第1項記載の両最外層と芯層との間
の少なくとも一方に挿入される層の直鎖状低密度ポリエ
チレン樹脂が、芯層に使用されている樹脂と同一である
、多層熱収縮性フィルム。 4)特許請求の範囲第1項記載の両最外層と芯層との間
の少なくとも一方に挿入される層の各厚みが、全体厚み
の7〜30%である、多層熱収縮性フィルム。
[Scope of Claims] 1) Both outermost layers are made of crystalline polypropylene resin with a melting point of 135 to 150°C, and the core layer has a density of 0.890 to 0.9.
10g/cm^3, the resin composition is made of a resin composition mainly composed of a linear low density polyethylene resin with a Vicat softening point of 60 to 80°C, and the above-mentioned crystals are included in at least one of the outermost layers and the core layer. A polypropylene resin and each resin selected from the above linear low density polyethylene resin are mixed in a weight ratio of 2:3 to 3:1, and
A barrier layer made of a resin composition in which the melt flow index of the crystalline polypropylene resin is higher than the melt flow index of the linear low density polyethylene resin is inserted, and at least one of the outermost layers as well as the barrier layer A multilayer heat-shrinkable film in which a lubricant is also added to the core layer. 2) The crystalline polypropylene resin of the layer inserted into at least one of the outermost layers and the core layer according to claim 1 is the same as the resin used for both outermost layers. Multilayer heat shrinkable film. 3) The linear low-density polyethylene resin of the layer inserted into at least one of the outermost layers and the core layer according to claim 1 is the same as the resin used for the core layer. , multilayer heat-shrinkable film. 4) A multilayer heat-shrinkable film, wherein the thickness of each layer inserted between at least one of the outermost layers and the core layer according to claim 1 is 7 to 30% of the total thickness.
JP63082066A 1987-10-21 1988-04-01 Multi-layer heat shrinkable film Expired - Lifetime JP2641242B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP63082066A JP2641242B2 (en) 1988-04-01 1988-04-01 Multi-layer heat shrinkable film
US07/584,635 US5086266A (en) 1987-10-21 1990-09-19 Automobile ac generator system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63082066A JP2641242B2 (en) 1988-04-01 1988-04-01 Multi-layer heat shrinkable film

Publications (2)

Publication Number Publication Date
JPH01253445A true JPH01253445A (en) 1989-10-09
JP2641242B2 JP2641242B2 (en) 1997-08-13

Family

ID=13764118

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63082066A Expired - Lifetime JP2641242B2 (en) 1987-10-21 1988-04-01 Multi-layer heat shrinkable film

Country Status (1)

Country Link
JP (1) JP2641242B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000047406A1 (en) * 1999-02-12 2000-08-17 Kureha Chemical Industry Co., Ltd. Packaging laminate
US6825276B2 (en) 2001-04-17 2004-11-30 Pliant Corporation Nonoriented stiff packaging film with superior tear properties
JP2010189052A (en) * 2009-02-20 2010-09-02 Toyo Seikan Kaisha Ltd Multilayered resin vessel for oily content

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000047406A1 (en) * 1999-02-12 2000-08-17 Kureha Chemical Industry Co., Ltd. Packaging laminate
CN1315642C (en) * 1999-02-12 2007-05-16 株式会社吴羽 Packaging laminate
US6825276B2 (en) 2001-04-17 2004-11-30 Pliant Corporation Nonoriented stiff packaging film with superior tear properties
JP2010189052A (en) * 2009-02-20 2010-09-02 Toyo Seikan Kaisha Ltd Multilayered resin vessel for oily content

Also Published As

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