JPS59114029A - Longitudinally uniaxially stretched sheet or film with excellent mechanical strength - Google Patents
Longitudinally uniaxially stretched sheet or film with excellent mechanical strengthInfo
- Publication number
- JPS59114029A JPS59114029A JP22543982A JP22543982A JPS59114029A JP S59114029 A JPS59114029 A JP S59114029A JP 22543982 A JP22543982 A JP 22543982A JP 22543982 A JP22543982 A JP 22543982A JP S59114029 A JPS59114029 A JP S59114029A
- Authority
- JP
- Japan
- Prior art keywords
- film
- sheet
- stretching
- stretched
- ethylene
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/005—Shaping by stretching, e.g. drawing through a die; Apparatus therefor characterised by the choice of materials
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised 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
- C08J2323/04—Homopolymers or copolymers of ethene
- C08J2323/08—Copolymers of ethene
Abstract
Description
【発明の詳細な説明】
本発明は縦−軸延伸シートもしくはフィルム(以下フィ
ルムと記す)に関する。さらに詳しくは縦方向、横方向
の引裂強度に優れた縦−軸延伸フィルムに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a longitudinally-axially stretched sheet or film (hereinafter referred to as film). More specifically, the present invention relates to a longitudinally-axially stretched film having excellent tear strength in the longitudinal and transverse directions.
従来、高圧法で製造される低密度ポIJ エチレン(以
下高圧法低密度ポリエチレンと称す)は、優れた衛生性
と耐湿性を有しておりまた光沢、透明性にも優れている
ため、包装材料を中心として広く使用されている。さら
に高圧法低密度ポリエチレンフィルムの機械的、光学的
、熱的性質等の向上を目的に縦−軸に延伸を施すことも
行なわれより高付加価値化が図られている。Conventionally, low-density polyethylene (hereinafter referred to as high-pressure low-density polyethylene) manufactured using a high-pressure method has excellent hygiene and moisture resistance, and is also excellent in gloss and transparency, so it is often used in packaging. Widely used as materials. Furthermore, in order to improve the mechanical, optical, thermal properties, etc. of high-pressure low-density polyethylene films, stretching is carried out along the longitudinal axis, thereby increasing added value.
−万、低圧法で製造される高密度ポリエチレン(以下低
圧法高密度ポリエチレンと称す)も優れた衛生性と耐湿
性を有しており包装材料を中心として広く使用されてい
る。さらに低圧法高密度ポリエチレンフィルムについて
も機械的、光学的性質等の向上を目的に縦−軸に延伸を
施すことも行なわれより高付加価値化が図られている。- High-density polyethylene produced by a low-pressure method (hereinafter referred to as low-pressure high-density polyethylene) also has excellent hygiene and moisture resistance, and is widely used mainly as packaging materials. Furthermore, low-pressure high-density polyethylene films are also stretched in the longitudinal direction for the purpose of improving mechanical and optical properties, thereby increasing added value.
しかし、−軸延伸フィルムは機械的性質において延伸方
向と圧延体方向には差異が生じ満足しうるものではない
。ポリエチレンフィルムを縦−軸に延伸することにより
付与される具体的な特性としては、縦方向の引張強度の
向上、縦方向の収縮特性の向上、光学的性質の向上、衝
撃強度の向上等がある。しかしポリエチレン−軸延伸フ
ィルムは一方向に非常に引裂けやすいという欠点を有し
ており包装フィルム等の各種使用時において破袋、コー
ナー破れ、割れ等の不良として現われ改良が望まれてい
る。However, the -axis stretched film is not satisfactory because there is a difference in mechanical properties between the stretching direction and the rolling body direction. Specific properties imparted by vertically stretching a polyethylene film include improved tensile strength in the longitudinal direction, improved shrinkage properties in the longitudinal direction, improved optical properties, and improved impact strength. . However, polyethylene-axially stretched films have the disadvantage of being extremely easy to tear in one direction, and this appears as defects such as torn bags, corner tears, cracks, etc. when used in various ways such as packaging films, and improvements are desired.
本発明はポリエチレン−軸延伸フィルムの持つ光学的、
機械的、熱的特性を損なうことなしに縦方向(MD)に
も横方向(TD)にも引裂けにくい一軸延伸フィルムを
得ることを目的に鋭意検討を進めた結果本発明に至った
。The present invention focuses on the optical properties of polyethylene-axially stretched film.
The present invention was achieved as a result of extensive research aimed at obtaining a uniaxially stretched film that is resistant to tearing in both the machine direction (MD) and the transverse direction (TD) without impairing its mechanical and thermal properties.
すなわち、本発明は長鎖分岐を実質的に有しない密度0
.91〜0.94のエチレン−αオレフィン共重合体を
シートもしくはフィルム状にした後、縦−軸方向にネッ
クイン率25%以下で2倍以上の延伸を施した延伸シー
トもしくはフィルムであり、かつ該延伸物のエルメンド
ルフ引裂強度が縦方向、横方向ともに60 Kg/m以
上を有することを特徴とする引裂強度の優れた縦−軸延
伸シートもしくはフィルム状物に関する1本発明におい
て用いられる長鎖分岐を実質的に有しないエチレン−α
オレフィン共重合体とは、遷移金属触媒を用い中低圧下
でエチレンとαオレフィンを共重合して得られる、高圧
法ポリエチレンと同程度の密度を有する樹脂、あるいは
高圧法ポリエチレンを得るのと同じような高圧下、高温
下で遷移金属触媒を用いてエチレンとαオレフィンを共
重合して得られる高圧法ポリエチレンと同程度の密度を
有する樹脂であるO
また本発明において用いられる縦−軸延伸の方法として
はロール間で引張力を加えながら延伸をおこなうロール
間延伸法、ロール間で圧下刃を加えて延伸する圧延法の
いずれを用いてもよいが用途によっては圧延法を用いる
万が熱的特性や光学的特性によりよい結果を示す。That is, the present invention has a density of 0, which has substantially no long chain branching.
.. A stretched sheet or film obtained by forming an ethylene-α olefin copolymer of 91 to 0.94 into a sheet or film, and then stretching it in the longitudinal-axial direction at a neck-in rate of 25% or more and at least twice as much, and 1. Long chain branches used in the present invention relating to a longitudinally-axially stretched sheet or film with excellent tear strength, characterized in that the stretched product has an Elmendorf tear strength of 60 Kg/m or more in both the longitudinal and transverse directions. Ethylene-α substantially free of
Olefin copolymer is a resin obtained by copolymerizing ethylene and α-olefin under medium-low pressure using a transition metal catalyst, and has a density similar to that of high-pressure polyethylene, or a resin similar to that obtained by high-pressure polyethylene. O is a resin having a density comparable to that of high-pressure polyethylene obtained by copolymerizing ethylene and α-olefin using a transition metal catalyst under high pressure and high temperature.Also, the longitudinal-axial stretching method used in the present invention For this purpose, either an inter-roll stretching method in which stretching is performed while applying a tensile force between rolls, or a rolling method in which stretching is performed by applying a reduction blade between rolls may be used, but depending on the application, the rolling method may be used depending on the thermal properties. It shows good results in terms of optical properties and optical properties.
また縦−軸延伸を施すに際、下式であられされるネック
イン率を25%以下にする必要があり、25%以上では
延伸フィルムの横方向の厚みムラが著しく悪くなり、ま
た縦方向の引裂強度が著しく低下するという問題があり
好適でない。In addition, when carrying out longitudinal-axial stretching, it is necessary to keep the neck-in rate calculated by the following formula below 25%; if it exceeds 25%, the thickness unevenness in the lateral direction of the stretched film will become extremely bad, and the This is not suitable because of the problem that the tear strength is significantly reduced.
さらに縦−軸延伸を施す際、延伸倍率は2倍以上は必要
であり、2倍以下では縦−伸延伸により付与される各種
特性の向上効果が少なく好適でない。Furthermore, when carrying out longitudinal-axis stretching, the stretching ratio must be at least 2 times, and if it is less than 2 times, the effect of improving various properties imparted by longitudinal-axis stretching is small and is not suitable.
以下実施例をもって本発明を説明する。The present invention will be explained below with reference to Examples.
実施例1.2
密度=0.921、MI=0.65のエチレン−αオレ
フィン共重合体を環状ダイより溶融押出しし、インフレ
ーション法により厚さ100μのフィルムを作製した。Example 1.2 An ethylene-α olefin copolymer having a density of 0.921 and an MI of 0.65 was melt-extruded through a circular die, and a film with a thickness of 100 μm was produced by an inflation method.
次にこの押出物に圧延法により縦−軸に2.6倍、4.
7倍の延伸を施した(ネックイン率:18%)。なお圧
延時におけるロール温度は50°Cであり潤滑液として
水を使用した。この縦−軸に延伸したフィルムの引裂強
度を測定した結果を第1表に示す。Next, this extrudate was rolled 2.6 times in the longitudinal direction, 4.
It was stretched 7 times (neck-in rate: 18%). The roll temperature during rolling was 50°C, and water was used as the lubricant. Table 1 shows the results of measuring the tear strength of the longitudinally stretched film.
(5)
実施例8
密度0.924、MI=l、09のエチレン−αオレフ
ィン共重合体を環状ダイより溶融押出シシ、インフレー
ション法により厚さ40μのフィルムを作製した。(5) Example 8 An ethylene-α olefin copolymer having a density of 0.924, MI=1, and 09 was melt-extruded through a circular die to produce a film with a thickness of 40 μm by an inflation method.
次にこの押出物に実施例1.2と同じ方法、条件で縦−
軸に4.8倍の延伸を施した(ネックイン率二16%)
。第1表に延伸フィルムの引裂強度を示す。Next, this extrudate was subjected to longitudinal treatment using the same method and conditions as in Example 1.2.
The shaft was stretched 4.8 times (neck-in rate: 216%)
. Table 1 shows the tear strength of the stretched film.
実施例4.5
密度0.928、MIに0.45のエチレン−αオレフ
ィン共重合体を環状ダイより溶融押出ししインフレーシ
ョン法により厚さ90μのフィルムを作製した。Example 4.5 An ethylene-α olefin copolymer having a density of 0.928 and an MI of 0.45 was melt-extruded from a circular die to produce a film with a thickness of 90 μm by an inflation method.
次にこの押出物に実施例1.2と同じ方法、条件で縦−
軸に8.0倍、5.0倍の延伸を施した(ネックイン率
=12%)。第1表に延伸フィルムの引裂強度を示す。Next, this extrudate was subjected to longitudinal treatment using the same method and conditions as in Example 1.2.
The shaft was stretched 8.0 times and 5.0 times (neck-in rate = 12%). Table 1 shows the tear strength of the stretched film.
実施例6
密度0.985、M I = 1.8のエチL/ :/
−(x(6)
オレフィン共重合体を円環状ダイより溶融押出しし厚さ
90μのフィルムを作製した。Example 6 Density 0.985, M I = 1.8 ethi L/ :/
-(x(6) The olefin copolymer was melt-extruded through a circular die to produce a film with a thickness of 90 μm.
次にこの押出物に圧延法により縦−軸5.3倍の延伸を
施した(ネックイン率:14%)。Next, this extrudate was stretched 5.3 times along the longitudinal axis by a rolling method (neck-in rate: 14%).
なお、圧延時におけるロール温度は75°Cであり潤滑
液として水を使用した。第1表に延伸フィルムの引裂強
度を示す。The roll temperature during rolling was 75°C, and water was used as the lubricant. Table 1 shows the tear strength of the stretched film.
実施例7
実施例1.2で作製した厚さ100μの押出フィルムに
圧延法により2.2倍の延伸を施した。圧延時のロール
温度は60°Cであり潤滑液は使用しない無潤滑圧延と
した(ネックイン率18%)。延伸フィルムの引裂強度
を第1表に示す。Example 7 The 100 μm thick extruded film produced in Example 1.2 was stretched 2.2 times by a rolling method. The roll temperature during rolling was 60°C, and non-lubricated rolling was performed without using lubricating fluid (neck-in rate 18%). The tear strength of the stretched film is shown in Table 1.
比較例1,2.8.4
密度0.924、M I = Q、 3の高圧法低密度
ポリエチレンを円環状ダイより溶融押出しし厚さ90μ
のフィルムを作製した。次にこの押出物に圧延法により
縦−軸に2倍、8倍、4倍、5倍の延伸を施した(ネッ
クイン率(7)
12%)。圧延時のロール温度は50”C!であり潤滑
液として水を使用した。第1表に延伸フィルムの引裂強
度を示す。Comparative Example 1, 2.8.4 High-pressure low-density polyethylene with a density of 0.924 and M I = Q, 3 was melt-extruded from an annular die to a thickness of 90 μm.
A film was produced. Next, this extrudate was stretched longitudinally by 2 times, 8 times, 4 times, and 5 times by a rolling method (neck-in rate (7): 12%). The roll temperature during rolling was 50"C! and water was used as the lubricant. Table 1 shows the tear strength of the stretched film.
比較例5.6.7
密度0.965、M I = 6.0の低圧法高密度ポ
リエチレンをTダイより溶融押出し、厚さ280μのシ
ートを作製した。次にこの押出物に圧延法により縦−軸
に8倍、4倍、5倍の延伸を施した(ネックイン率:4
%)。圧延時のロール温度は85℃であり潤滑液として
水を使用した。第1表に延伸フィルムの引裂強度を示す
。Comparative Example 5.6.7 Low-pressure high-density polyethylene with a density of 0.965 and M I = 6.0 was melt-extruded from a T-die to produce a sheet with a thickness of 280 μm. Next, this extrudate was stretched longitudinally by 8 times, 4 times, and 5 times by a rolling method (neck-in ratio: 4
%). The roll temperature during rolling was 85°C, and water was used as the lubricant. Table 1 shows the tear strength of the stretched film.
第 1 表
注)1.引裂強度の測定はJI8P−8116で行なっ
た。Table 1 Note) 1. The tear strength was measured using JI8P-8116.
2、MD:延伸方向(縦方向)
TD:反延伸方向(横方向)
(9)
第1表に示した実施例、比較例より明らかなように高圧
法低密度ポリエチレンよりなるフィルムもしくはシート
状物に縦−軸延伸を施したフィルムもしくはシートは横
方向の引裂強度が極めて低くなり、しかも延伸により付
与される特性をより高めるために延伸倍率を高くすれば
するほど横方向の引裂強度は低くなる。また低圧法高密
度ポリエチレンよりなるフィルムもしくはシート状物に
縦−軸延伸を施したフィルムもしくはシートは縦方向の
引裂強度が極めて低くなる。−万、本発明でいうエチレ
ン−αオレフィン共重合体からなる縦−軸延伸フィルム
もしくはシートは縦方向、横方向ともに60 b/ca
r以上のすぐれた引裂強度を有しており本発明の効果は
明白である。2. MD: Stretching direction (longitudinal direction) TD: Counter-stretching direction (horizontal direction) (9) As is clear from the examples and comparative examples shown in Table 1, a film or sheet-like product made of high-pressure low-density polyethylene A film or sheet that has been subjected to longitudinal-axial stretching has extremely low tear strength in the transverse direction, and the higher the stretching ratio to enhance the properties imparted by stretching, the lower the tear strength in the transverse direction. . Furthermore, a film or sheet made of low-pressure high-density polyethylene that is subjected to longitudinal-axis stretching has extremely low tear strength in the longitudinal direction. -10,000, the longitudinally-axially stretched film or sheet made of the ethylene-α olefin copolymer referred to in the present invention has a capacity of 60 b/ca in both the longitudinal and transverse directions.
It has an excellent tear strength of r or more, and the effects of the present invention are obvious.
(10完)(10 complete)
Claims (1)
エチレン−αオレフィン共重合体をシートもしくはフィ
ルム状にした後、縦−軸方向にネックイン率25π以下
で2倍以上の延伸を施した延伸シートもしくはフィルム
であり、かつ該延伸物のエルメンドルフ引裂強度がM、
D方向およびTD方向ともに60Kg/crR以上で
あることを特徴とする引裂強度の優れた縦−軸延伸シー
トもしくはフィルム。After forming an ethylene-α olefin copolymer having a density of 0.91 to 0.94 with substantially no long chain branching into a sheet or film, stretching it in the longitudinal-axial direction at a neck-in rate of 25π or less by a factor of 2 or more. Stretched sheet or film, and the Elmendorf tear strength of the stretched product is M,
A longitudinally-axially stretched sheet or film with excellent tear strength, characterized by having a tear strength of 60 Kg/crR or more in both the D direction and the TD direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22543982A JPS59114029A (en) | 1982-12-21 | 1982-12-21 | Longitudinally uniaxially stretched sheet or film with excellent mechanical strength |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22543982A JPS59114029A (en) | 1982-12-21 | 1982-12-21 | Longitudinally uniaxially stretched sheet or film with excellent mechanical strength |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59114029A true JPS59114029A (en) | 1984-06-30 |
Family
ID=16829377
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22543982A Pending JPS59114029A (en) | 1982-12-21 | 1982-12-21 | Longitudinally uniaxially stretched sheet or film with excellent mechanical strength |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59114029A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6956088B2 (en) * | 2001-07-19 | 2005-10-18 | Univation Technologies, Llc | Polyethylene films with improved physical properties |
US7172816B2 (en) | 2001-07-19 | 2007-02-06 | Univation Technologies, Llc | High tear films from hafnocene catalyzed polyethylenes |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56126A (en) * | 1979-06-08 | 1981-01-06 | Mobil Oil | Thermoplastic uniaxial drawn film |
-
1982
- 1982-12-21 JP JP22543982A patent/JPS59114029A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56126A (en) * | 1979-06-08 | 1981-01-06 | Mobil Oil | Thermoplastic uniaxial drawn film |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6956088B2 (en) * | 2001-07-19 | 2005-10-18 | Univation Technologies, Llc | Polyethylene films with improved physical properties |
US7172816B2 (en) | 2001-07-19 | 2007-02-06 | Univation Technologies, Llc | High tear films from hafnocene catalyzed polyethylenes |
US7179876B2 (en) | 2001-07-19 | 2007-02-20 | Univation Technologies, Llc | High tear films from hafnocene catalyzed polyethylenes |
US8399581B2 (en) | 2001-07-19 | 2013-03-19 | Univation Technologies, Llc | Polyethylene films with improved physical properties |
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