JPH0318655B2 - - Google Patents

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Publication number
JPH0318655B2
JPH0318655B2 JP9191883A JP9191883A JPH0318655B2 JP H0318655 B2 JPH0318655 B2 JP H0318655B2 JP 9191883 A JP9191883 A JP 9191883A JP 9191883 A JP9191883 A JP 9191883A JP H0318655 B2 JPH0318655 B2 JP H0318655B2
Authority
JP
Japan
Prior art keywords
density polyethylene
heat
stretching
ethylene
linear low
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.)
Expired
Application number
JP9191883A
Other languages
Japanese (ja)
Other versions
JPS59215828A (en
Inventor
Hisashi Shimizu
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.)
Gunze Ltd
Original Assignee
Gunze 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 Gunze Ltd filed Critical Gunze Ltd
Priority to JP9191883A priority Critical patent/JPS59215828A/en
Publication of JPS59215828A publication Critical patent/JPS59215828A/en
Publication of JPH0318655B2 publication Critical patent/JPH0318655B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/005Shaping by stretching, e.g. drawing through a die; Apparatus therefor characterised by the choice of materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037Other properties
    • B29K2995/0049Heat shrinkable
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037Other properties
    • B29K2995/0063Density
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は直鎖状低密度ポリエチレンを用いてな
る熱収縮性フイルムに関する。 従来、ポリエチレン系重合体の熱収縮性フイル
ムは未延伸フイルム製膜後、改めて再加熱して行
なう、通常のテンター等による延伸ができにくい
ので、主にチユーブラー押出時の溶融状態の樹脂
を冷却しつつブローアツプ及び引取速度を好まし
い条件に設定してインフレ方式で配向を生じしめ
る方法により製造されているが、このものは強度
が不足したり、収縮可能温度範囲が狭いために熱
収縮操作を行ないにくかつたり、収縮応力が小さ
いため被包装物への密着状態が十分でないなどの
問題があつた。 こうした問題を解決するために、通常の延伸が
可能な架橋ポリエチレンからなる熱収縮性フイル
ムが市場に出回つており、各メーカーは斯る架橋
ポリエチレンを好んで用いているが、このものは
溶断シール等の熱シール性に乏しい上に、再生使
用に難点がある等の若干の問題点を有していた。 そこで本発明者らは直鎖状低密度ポリエチレン
に注目し、種種検討を繰り返した結果、斯る直鎖
状低密度ポリエチレンに特定の重合体を添加し、
製膜することにより延伸性に優れた好適な熱収縮
性フイルムを提供することを見出し、本発明に至
つたもので、その特徴とするところは直鎖状低密
度ポリエチレンと変性ポリオレフインからなる薄
膜を延伸してなる熱収縮性フイルムを見出した点
にあり、更にその特徴とするところは直鎖状低密
度ポリエチレンと変性ポリオレフインとエチレン
系重合体からなる薄膜を延伸してなる熱収縮性フ
イルムを見出した点にある。 本発明に係る直鎖状低密度ポリエチレンとは略
一定の長さの側鎖が適当に存在する低密度のもの
をいう。ポリエチレンは通常不規則な側鎖が多数
あるものを低密度ポリエチレンといい、側鎖が短
く少ないものを中、高密度ポリエチレンといつて
いるが、一般に前者は高圧法により、後者は中、
低圧法により製造されている。ところが本発明に
係るポリエチレンは通常中、低圧法で製造されつ
つ、人為的に側鎖を導入することにより、嵩ばつ
た分子となつて詰まり方が比較的疎となり、直鎖
状で低密度のものが製造される。この際、側鎖を
導入するためには例えばブテン−1等を加えてコ
ポリマー状にしてもよいし、その他適宜の方法に
よつて側鎖を導入すればよく、その製造方法も特
に制限はない。 変性ポリオレフインとはポリエチレン(前記し
た直鎖状低密度ポリエチレンも入る)、エチレン
−酢酸ビニル共重合体、エチレン・プロピレン共
重合体等のポリオレフインにフマル酸、マレイン
酸及びその無水物等の不飽和カルボン酸、または
その誘導体から選ばれた少なくとも1種のモノマ
ーの適宜の必要量をグラフト共重合せしめてなる
もので、上記モノマーの好ましい範囲は10-4〜10
重量%、更には10-3〜5重量%であるが、この値
は限定されるものではない。斯る変性ポリオレフ
インは変性ポリオレフインのみで構成されていて
もよく、また変性ポリオレフインに未変性ポリオ
レフイン及び/または第3成分をその特徴が失わ
れない範囲で適宜に混合してなる混合体であつて
もよい。本発明に係るエチレン系重合体とは前記
した直鎖状低密度ポリエチレン及び変性ポリオレ
フインを除くものを云い、例えばエチレン−酢酸
ビニル共重合体、エチレン・プロピレン共重合
体、通常の低、中、高密度ポリエチレン、エチレ
ン系アイオノマー等を挙げることができ特に制限
はない。 変性ポリオレフインを添加する理由は直鎖状低
密度ポリエチレン単独では延伸性に劣り、厚み精
度が不十分で厚薄のバラツキが多くみられたので
こうした欠点を改良するたである。更にポリエチ
レン系重合体を加えることにより延伸性も一層向
上し、収縮率も大幅に向上することが確認され本
発明に及んだのである。 熱収縮性フイルムを製造するためには通常工業
的に用いられる溶融押出法が好適であるが、その
他周知の方法でよく、例えば溶融状態の樹脂を急
令していつたん未延伸フイルムを製膜し、しかる
後斯る未延伸フイルムを再加熱して延伸を行なえ
ばよい。延伸は例えば縦延伸、横延伸、縦横2軸
延伸等を行なえばよく、ロール延伸機、テンター
方式、チユーブラー方式等により、1軸、遂次2
軸、同時2軸等好ましい状態に延伸すればよい。 斯る延伸とはいわゆる押出ブローアツプ時に起
る配向とは異なり、連続式で行なうにしても製膜
工程と分けて行なうものである。 この際、本発明の熱収縮性フイルムには帯電防
止剤その他の添加剤、充填剤を必要に応じ使用す
ることはいつこうにかまわない。また、本発明の
用途はキヤツプシール、シユリンクラベル、その
他一般包装用等多岐に渡り、特に制限を受けるも
のでないことは勿論である。 本発明は以上の通りであり、本発明による熱収
縮性フイルムは製膜後行なう通常の延伸を行なつ
ても、破れ、厚さ精度不良等による問題点も生ず
ることなく、極めて延伸性に優れた均一な厚さの
ものが得られ、更にその熱収縮率についても高い
値を示した。このことからも本発明の格別顕著な
効果がうかがわれ、本発明は従来、問題点を多く
残していた通常の延伸法で、新規な熱収縮性フイ
ルムの提供を可能にしたものであり、今後多くの
需要が期待されている。 〈実施例 1〉 直鎖状でかつ略一定の長さの側鎖が適当にある
密度0.920、MI2.1の直鎖状低密度ポリエチレンに
表(1)記載の各種重合体を添加してTダイによりチ
ルロールで急令し、フラツト状に押出製膜した未
延伸フイルムを表(1)記載の条件により縦方向にロ
ール延伸を行ない、しかる後横方向にテンター延
伸を行なう、いわゆる遂次2軸延伸法により各種
の熱収縮性フイルムを得た。斯る熱収縮性フイル
ムの物性は同じく表(1)に記載し、あわせて直鎖状
低密度ポリエチレンのみからなる熱収縮性フイル
ムも比較例(1)として掲示した。 尚、表(1)における変性ポリオレフインのうち実
験No.(1)、同(4)、同(5)、同(6)、のものは低密度ポリ
エチレンをベースに無水マレイン酸をグラフト共
重合せしめたもの、実験No.(2)、同(3)は直鎖状低密
度ポリエチレンをベースに無水マレイン酸をグラ
フト共重合せしめたものである。 また、ポリエチレン系重合体のうち実験No.(3)、
同(4)のものは酢酸ビニル含有量15重量%、MI=
1.5のエチレン−酢酸ビニル共重合体、実験No.(5)
のものはエチレン含有量6.0重量%のエチレン−
プロピレン共重合体、実験No.(6)ものは低密度ポリ
エチレンである。
The present invention relates to a heat-shrinkable film made of linear low-density polyethylene. Conventionally, heat-shrinkable films made from polyethylene polymers are difficult to stretch using a normal tenter, which requires reheating after forming an unstretched film, so the resin is mainly cooled in a molten state during tubular extrusion. However, this method does not have enough strength or has a narrow shrinkable temperature range, so it is difficult to perform heat shrinking. There were problems such as shrinkage and insufficient adhesion to the packaged item due to the small shrinkage stress. To solve these problems, heat-shrinkable films made of cross-linked polyethylene that can be stretched normally are on the market, and manufacturers prefer to use such cross-linked polyethylene. It had some problems, such as poor heat sealability and difficulty in recycling. Therefore, the present inventors focused on linear low-density polyethylene, and as a result of repeated studies, we added a specific polymer to such linear low-density polyethylene,
It was discovered that a suitable heat-shrinkable film with excellent stretchability could be provided by forming a film, leading to the present invention.The feature is that a thin film made of linear low-density polyethylene and modified polyolefin The company discovered a heat-shrinkable film made by stretching the film, and its unique feature is that it discovered a heat-shrinkable film made by stretching a thin film made of linear low-density polyethylene, modified polyolefin, and ethylene polymer. It is at the point. The linear low-density polyethylene according to the present invention refers to a low-density polyethylene in which side chains of approximately constant length are appropriately present. Polyethylene with a large number of irregular side chains is usually called low density polyethylene, and those with short and few side chains are called medium or high density polyethylene, but the former is generally produced using a high-pressure process, and the latter is produced using a medium or high density polyethylene.
Manufactured by low pressure method. However, the polyethylene according to the present invention is usually produced by a medium-low pressure method, but by artificially introducing side chains, it becomes a bulky molecule with relatively sparse clogging, and has a linear, low-density structure. something is manufactured. At this time, in order to introduce a side chain, for example, butene-1 or the like may be added to form a copolymer, or the side chain may be introduced by any other appropriate method, and there are no particular restrictions on the manufacturing method. . Modified polyolefins are polyolefins such as polyethylene (including the above-mentioned linear low-density polyethylene), ethylene-vinyl acetate copolymers, ethylene-propylene copolymers, etc., and unsaturated carboxylates such as fumaric acid, maleic acid, and their anhydrides. It is obtained by graft copolymerizing an appropriate amount of at least one monomer selected from acids or derivatives thereof, and the preferred range of the monomer is 10 -4 to 10
% by weight, more preferably from 10 -3 to 5% by weight, but this value is not limited. Such modified polyolefin may be composed only of modified polyolefin, or it may be a mixture formed by appropriately mixing modified polyolefin with unmodified polyolefin and/or a third component to the extent that its characteristics are not lost. good. The ethylene polymer according to the present invention refers to those excluding the above-mentioned linear low density polyethylene and modified polyolefin, such as ethylene-vinyl acetate copolymer, ethylene-propylene copolymer, and ordinary low, medium, and high density polyethylene. Density polyethylene, ethylene ionomer, etc. can be mentioned, but there are no particular limitations. The reason for adding modified polyolefin is to improve these drawbacks, since linear low-density polyethylene alone had poor stretchability, insufficient thickness accuracy, and many variations in thickness. Furthermore, it was confirmed that by adding a polyethylene polymer, the stretchability was further improved and the shrinkage rate was also significantly improved, leading to the present invention. Melt extrusion, which is usually used industrially, is suitable for producing heat-shrinkable films, but other well-known methods may also be used. However, the unstretched film may then be reheated and stretched. Stretching may be carried out, for example, by longitudinal stretching, transverse stretching, biaxial stretching in longitudinal and lateral directions, etc., and can be carried out uniaxially, sequentially in two directions, etc. using a roll stretching machine, tenter method, tubular method, etc.
It may be stretched in a preferred state such as axially or simultaneously biaxially. Such stretching is different from the orientation that occurs during so-called extrusion blow-up, and is performed separately from the film forming process even if it is carried out continuously. At this time, antistatic agents, other additives, and fillers may be used in the heat-shrinkable film of the present invention as needed. Further, the present invention can be used in a wide variety of applications, such as cap stickers, shrink labels, and other general packaging, and is, of course, not subject to any particular limitations. The present invention is as described above, and the heat-shrinkable film according to the present invention has extremely excellent stretchability without causing any problems such as tearing or poor thickness accuracy even if it is subjected to normal stretching after film formation. A product with a uniform thickness was obtained, and its heat shrinkage rate also showed a high value. This also shows that the present invention has a particularly remarkable effect, and the present invention has made it possible to provide a novel heat-shrinkable film using the conventional stretching method, which had many problems in the past. Much demand is expected in the future. <Example 1> Various polymers listed in Table (1) were added to linear low-density polyethylene with a density of 0.920 and an MI of 2.1, which is linear and has side chains of approximately constant length. An unstretched film that is extruded into a flat shape by extrusion using a chill roll through a die is subjected to roll stretching in the longitudinal direction under the conditions listed in Table (1), and then tenter stretching in the transverse direction, which is the so-called sequential biaxial method. Various heat-shrinkable films were obtained by the stretching method. The physical properties of such a heat-shrinkable film are also listed in Table (1), and a heat-shrinkable film made only of linear low-density polyethylene is also listed as Comparative Example (1). In addition, among the modified polyolefins in Table (1), those in Experiment Nos. (1), (4), (5), and (6) are made by graft copolymerizing maleic anhydride onto a base of low-density polyethylene. Experiment No. (2) and Experiment No. (3) were made by graft copolymerizing maleic anhydride onto a linear low-density polyethylene base. In addition, among polyethylene polymers, Experiment No. (3),
The same (4) has a vinyl acetate content of 15% by weight, MI=
1.5 ethylene-vinyl acetate copolymer, Experiment No. (5)
The one with ethylene content is 6.0% by weight.
The propylene copolymer, Experiment No. (6), is low density polyethylene.

【表】 〈実施例 2〉 実施例1と同様の直鎖状低密度ポリエチレンに
表(2)記載の各種重合体を添加して、環状ダイによ
り水冷インフレーシヨン方式により押出製膜した
未延伸フイルムを、一旦巻き取り、しかる後チユ
ーブラー法による同時2軸延伸法により各種の熱
収縮性フイルムを得た。斯る熱収縮性フイルムの
物性は同じく表(2)に記載し、併せて直鎖状低密度
ポリエチレンのみからなる熱収縮性フイルムも比
較例(2)として掲示した。 尚、表(1)における変性ポリオレフインのうち実
験No.(1)のものは直鎖状低密度ポリエチレンベー
ス、実験No.(2)、同(3)、同(4)のものは低密度ポリエ
チレンベースの実施例1と同じものである。また
ポリエチレン系重合体のうち、実験No.(1)、同(2)の
ものは実施例(1)と同じエチレン−酢酸ビニル共重
合体、実験No.(3)のものは実施例1と同じエチレン
−プロピレン共重合体、実験No.(4)のものは低密度
ポリエチレンである。
[Table] <Example 2> An unstretched film obtained by adding various polymers listed in Table (2) to the same linear low-density polyethylene as in Example 1 and extruding it using a water-cooled inflation method using an annular die. The film was once wound up and then subjected to simultaneous biaxial stretching using the tubular method to obtain various heat-shrinkable films. The physical properties of such a heat-shrinkable film are also listed in Table (2), and a heat-shrinkable film made only of linear low-density polyethylene is also listed as Comparative Example (2). Of the modified polyolefins in Table (1), those in experiment No. (1) are based on linear low-density polyethylene, and those in experiment Nos. (2), (3), and (4) are based on low-density polyethylene. This is the same as the base example 1. Among the polyethylene polymers, those in Experiment No. (1) and (2) are the same ethylene-vinyl acetate copolymer as in Example (1), and those in Experiment No. (3) are the same as in Example 1. The same ethylene-propylene copolymer used in Experiment No. (4) is low-density polyethylene.

【表】【table】

【表】 以上の表(1)、表(2)からも明らかな通り、本発明
の熱収縮性フイルムは延伸性に優れるために厚さ
制度も良好で、しかもその熱収縮率も極めて高
く、低温においても比較的高い値を示し、熱収縮
可能温度範囲の広いことをうかがわせるものであ
つた。
[Table] As is clear from Tables (1) and (2) above, the heat-shrinkable film of the present invention has excellent stretchability and good thickness accuracy, and its heat-shrinkage rate is also extremely high. It showed a relatively high value even at low temperatures, suggesting that the temperature range in which heat shrinkage is possible is wide.

Claims (1)

【特許請求の範囲】 1 直鎖状低密度ポリエチレンと変性ポリオレフ
インからなる薄膜を延伸してなる熱収縮性フイル
ム。 2 直鎖状低密度ポリエチレンと変性ポリオレフ
インとエチレン系重合体からなる薄膜を延伸して
なる熱収縮性フイルム。 3 エチレン系重合体が低密度ポリエチレン、エ
チレン−プロピレン共重合体、エチレン−酢酸ビ
ニル共重合体のうちから選ばれた少なくとも1種
の高分子材料である特許請求の範囲第2項記載の
熱収縮性フイルム。
[Claims] 1. A heat-shrinkable film made by stretching a thin film made of linear low-density polyethylene and modified polyolefin. 2. A heat-shrinkable film made by stretching a thin film made of linear low-density polyethylene, modified polyolefin, and ethylene polymer. 3. The heat shrinkage according to claim 2, wherein the ethylene polymer is at least one polymeric material selected from low density polyethylene, ethylene-propylene copolymer, and ethylene-vinyl acetate copolymer. sex film.
JP9191883A 1983-05-24 1983-05-24 Heat-shrinkable film Granted JPS59215828A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9191883A JPS59215828A (en) 1983-05-24 1983-05-24 Heat-shrinkable film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9191883A JPS59215828A (en) 1983-05-24 1983-05-24 Heat-shrinkable film

Publications (2)

Publication Number Publication Date
JPS59215828A JPS59215828A (en) 1984-12-05
JPH0318655B2 true JPH0318655B2 (en) 1991-03-13

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP9191883A Granted JPS59215828A (en) 1983-05-24 1983-05-24 Heat-shrinkable film

Country Status (1)

Country Link
JP (1) JPS59215828A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IN2014CN02109A (en) 2011-09-23 2015-05-29 Dow Global Technologies Llc

Also Published As

Publication number Publication date
JPS59215828A (en) 1984-12-05

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