JPS587329A - Manufacture of polyolefin film - Google Patents

Manufacture of polyolefin film

Info

Publication number
JPS587329A
JPS587329A JP56105968A JP10596881A JPS587329A JP S587329 A JPS587329 A JP S587329A JP 56105968 A JP56105968 A JP 56105968A JP 10596881 A JP10596881 A JP 10596881A JP S587329 A JPS587329 A JP S587329A
Authority
JP
Japan
Prior art keywords
polyethylene
film
polypropylene
propylene
crystalline
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
JP56105968A
Other languages
Japanese (ja)
Other versions
JPS6140176B2 (en
Inventor
Tadao Ishibashi
忠夫 石橋
Yoichi Kugimiya
釘宮 陽一
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.)
JNC Corp
Original Assignee
Chisso Corp
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 Chisso Corp filed Critical Chisso Corp
Priority to JP56105968A priority Critical patent/JPS587329A/en
Publication of JPS587329A publication Critical patent/JPS587329A/en
Publication of JPS6140176B2 publication Critical patent/JPS6140176B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00Producing flat articles, e.g. 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain the titled film efficiently that is excellent in transparency, rigidity, easy heat sealability and useful for common packaging etc. by melting and extruding specific crystalline propylene-alpha-olefin copolymer and high density polyethylene under a specific condition. CONSTITUTION:Where polypropylene is crystalline propylene-alpha-olefin copolymer containing 70% or more of propylene component when the crystalline melting point is 150 deg.C or lower, polyethylene is high density polyethylene having a density 0.945 or more and a flow ratio 15 or less and the ratio of the melt index (MI) of polyethylene to the melt flow rate (MFR) of polypropylene is (MI/MFR)>=1.2, the composition composed of 96-85% by weight of polypropylene and 4-15% by weight of polyethylene is melted and extruded at 180-250 deg.C and then cooled quickly to 50 deg.C or lower to obtain the desired film.

Description

【発明の詳細な説明】 本発明はポリオレフィンフィルムのlIA造方法に関す
る。更に詳しくは、遥@性及び剛性の優れた低電ヒート
シーー性ポリオレフィンフィルの調造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for making IIA of polyolefin films. More specifically, the present invention relates to a method for preparing a low-electricity heat-sealable polyolefin fill having excellent properties and rigidity.

近年、エチレン−プロピレンランダム共重合体、エチレ
ン−プロピレン−1テン−1共IK倉体、プロピレン−
ブテン−1共重合体等のプロピレンを主体とする結晶性
プロピレン−一−オレフイン共重倉体はその優れた透明
性、耐衝撃fk訃よび低温ヒートシーJhIk螢の特性
を生かしうζネート層、一般包装用等の他広くフイ身ム
層辿にII!JIlされている。
In recent years, ethylene-propylene random copolymer, ethylene-propylene-1ten-1 copolymer IK Kurata, propylene-
Crystalline propylene-1-olefin copolymer bodies mainly composed of propylene, such as butene-1 copolymer, have a zeta layer and general packaging that take advantage of their excellent transparency, impact resistance, and low-temperature heat-sea properties. In addition to other uses, it can also be used for a wide range of people! JIl has been done.

曽晶性プロピレンーα−オレフィン共重金体中のスモノ
マーiit分會量が増すにりれて、共重合体の麹晶融点
位低下し、フィルAF)低温ヒーFシーkfllllL
び高速ヒートシーに性が肉上するが、MIIKフィAA
の剛性が低下する。例えば、未嬌伸フィルムの場合、結
晶融点が164℃の結晶性ボップルピレンフィルムに比
して、結JJk点カ150〜140Cf)麹晶性エチレ
ンープロピレンツンダA共重金体は剛さが2o〜4o*
4b低下する。従ってに−)シール性の改善によってl
lli袋作業や自動包装を^造化する目的で共重合体中
のコモノマー含量を増すことは、−性の低下による製膜
時のシワ、巻取時の巻き締9による両趨部の肥厚等のフ
ィルムの平面性不良を来たすだけでなく、フィル^のり
にミや延びKよる印刷、製袋、自動完膚等の作業性を低
下させるという問題を発生する。この剛さはフィルムの
厚さが薄いはど加工特性として1簀となり、上記剛性の
低下は省資源を目的とするフィルムの薄肉化への大きな
障書となっている。
As the amount of smonomer iit in the crystalline propylene-α-olefin copolymer increases, the koji crystal melting point of the copolymer decreases and
Although the sex increases due to high speed heat sea, MIIK FiAA
stiffness decreases. For example, in the case of an unstretched film, compared to a crystalline bopple pyrene film whose crystal melting point is 164°C, the koji crystalline ethylene-propylene-Zunda A coheavy metal body has a crystalline melting point of 150 to 140 Cf). 2o~4o*
4b decreases. Therefore, by improving sealing performance, l
Increasing the content of the comonomer in the copolymer for the purpose of making plastic bags and automatic packaging can lead to wrinkles during film formation due to a decrease in film properties, thickening of both ends due to tightening during winding, etc. This not only causes poor flatness of the film, but also causes problems such as smudges and elongation of the film, which reduces workability in printing, bag making, automatic wrapping, etc. This stiffness is due to the film's thin edge processing characteristics, and the decrease in stiffness is a major hindrance to thinning the film for the purpose of resource saving.

本発明者らは、結晶性グロビレンーα−オレフィン共重
合体の優れた透明性、及び低温ヒートシール性を損うこ
となく剛性を改善することを目的に種々検討した結果、
結晶性プロピレアーα−オレフィン共重合体に特定の高
密度ポリエチレンを特定の割合で混合した組成物を特定
の条件で製膜することによって上記目的が達せられるこ
とを知り本発明を完成するに到った。
As a result of various studies aimed at improving the rigidity of the crystalline globylene-α-olefin copolymer without impairing its excellent transparency and low-temperature heat sealability, the present inventors found that
We learned that the above object can be achieved by forming a film under specific conditions from a composition in which a crystalline propyleae α-olefin copolymer is mixed with a specific high-density polyethylene in a specific ratio, which led us to complete the present invention. Ta.

すなわち本発明は、ポリプロピレンが、結晶融点150
℃以下、プロピレン成分を70チ以上會有する結晶性プ
ロピレン−a−オレフイ/共重合体でToj+、ポリエ
チレンが、密度α?45以上、フにジオが15以下の高
密度ポリエチレンで1t)n、かつ、該ポリエチレンの
メにシインデックス(MI )と該ポリ10ピレンのメ
^ドアー−レート(MFR)の比が(MI/MPi)≧
12であるようなポリプロピレン96〜85重量−とポ
リエチレン4〜15重量−とから成る駆威物を、180
〜250CでIFlk押出し、50C以下に急冷するこ
とを特徴とする透l#法及び剛性に優した轟ヒートシー
ル性ポリオレプインフィルのm進方法である。
That is, in the present invention, polypropylene has a crystal melting point of 150
℃ or less, Toj+ is a crystalline propylene-a-olefin/copolymer having a propylene component of 70 or more, and polyethylene has a density α? 45 or more, and the carbon dioxide is 15 or less, and the ratio of the media index (MI) of the polyethylene to the media rate (MFR) of the poly-10 pyrene is (MI/ MPi)≧
A propellant consisting of 96 to 85 weight of polypropylene such as 12 and 4 to 15 weight of polyethylene was added to 180
These are the transparent l# method, which is characterized by IFlk extrusion at ~250C and rapid cooling to 50C or less, and the m-adic method of high-stiffness heat-sealable polyolep infill.

本発明で用いるポリプロピレンは、プロピレン成分を7
0重量−以上含有する績品性グロビレンーα−オレフィ
ン共重合体であって、結晶融点が150以下でなければ
ならない。プロピレン成分が70重量tsK適しないと
、得られたフィルムはブロッキングを起し易く、結晶融
点が15DCを趨えると低温ヒートシーに性及び高速ヒ
ートシール性が著しく低下し、いずれも好ましくない。
The polypropylene used in the present invention has a propylene component of 7
The globylene-α-olefin copolymer must contain 0 weight or more, and must have a crystal melting point of 150 or less. If the propylene component is not suitable for 70 weight tsK, the obtained film is likely to cause blocking, and if the crystal melting point exceeds 15 DC, low temperature heat sealability and high speed heat sealability will be significantly reduced, both of which are unfavorable.

このようなポリプロピレンは、主成分のプロピレンとコ
モノマーのエチレンあるいは炭素数4〜8のα−オレフ
ィンを例えばチーグラーΦナツメ系触媒等を用いた公知
の方法によってランダム共重合させることにより祷るこ
とができる。このような共重合体の例として、エチレン
−フロピレン共重合体、 7 a ヒV ン7’ f 
ノー1共重合体、エチレン−プロピレン−ブテン−1三
元共重合体等が挙げられる。
Such polypropylene can be produced by randomly copolymerizing the main component propylene and the comonomer ethylene or an α-olefin having 4 to 8 carbon atoms by a known method using, for example, a Ziegler Φ jujube catalyst. . Examples of such copolymers include ethylene-propylene copolymers,
Examples thereof include No. 1 copolymer, ethylene-propylene-butene-1 terpolymer, and the like.

本発明において結晶融点(以下Tmと略称する)とは、
走食型差勧熱−゛計を用いて窒素雰囲気中で試料を10
℃/分の速度で昇温させて得られる結晶のamに伜な9
吸熱カーブのピーク温度をさす。Tmは、低密度ポリエ
チレンでは105〜112℃、高密度ボチエチレンでは
124〜162℃、結晶性ポリプロピレンでは162〜
165℃である。また、結晶性プロピレン−α−オレフ
イ/共重合体では、コモノマー成分の含有量カ増すとT
mが低下し、ゴチレンープロピレンツンダム共重合体の
場合、共重合体中のエチレン成分が25重量−を超える
とTaは150℃以下Kする。なおエチレン−プロピV
ンfElツク共重合体の如く、ブロック的に共重合した
もののTm#′i、−毅[150C以上でl)、得られ
るフィルムの剛性は尚いが透明性が著しく劣るので本I
AwAに轄使用できない。
In the present invention, the crystal melting point (hereinafter abbreviated as Tm) means:
A sample was heated for 10 minutes in a nitrogen atmosphere using a running-type differential thermometry meter.
The crystals obtained by increasing the temperature at a rate of ℃/min are 9
Refers to the peak temperature of the endothermic curve. Tm is 105-112°C for low-density polyethylene, 124-162°C for high-density polyethylene, and 162-162°C for crystalline polypropylene.
The temperature is 165°C. In addition, in crystalline propylene-α-olefin/copolymer, when the content of the comonomer component increases, T
m decreases, and in the case of a gotylene-propylene Sundam copolymer, when the ethylene component in the copolymer exceeds 25% by weight, Ta decreases to 150° C. or lower. In addition, ethylene-propy V
When block copolymerization is performed, such as Tm#'i, -Tsu [1 at 150 C or higher], the resulting film has better rigidity but significantly lower transparency, so this book I
Cannot be used under AwA.

本発明で用いるポリエチレンは、密度が1945以上、
7o−レシオが15以下の高密度ポリエチレンである。
The polyethylene used in the present invention has a density of 1945 or more,
High-density polyethylene with a 7o-ratio of 15 or less.

ポリエチレンの密度がa945未満では剛性向上の効果
が不充分、であシ、7Il!−レシオが15を超えると
フィルムの透明性が低下し、いずれも好ましくない。
If the density of polyethylene is less than a945, the effect of improving rigidity is insufficient. - If the ratio exceeds 15, the transparency of the film decreases, which is not preferable.

本孔明を効果的に災施するには、密度0.955以上テ
フローレシオ8〜12の高密度ポリエチレンが%に好ま
しく用いられる。
In order to effectively apply this method, high-density polyethylene having a density of 0.955 or more and a teflow ratio of 8 to 12% is preferably used.

零発f!A#cおいて密度とは、JISK6760(ポ
リエチレン試験方法)に基いて測定された密度をいう。
Zero shot f! In A#c, the density refers to the density measured based on JIS K6760 (polyethylene test method).

またフローレシオ(以下F凡と略称するンとは、JI8
 K67600メルトインデックス(以下MIと略称す
る)の測定法において、1a81g#)、荷重を用いて
得られた値(Mllo)を通常の2.16輪の荷重を用
いて得られた値(MI)で除して得られる商をいう。す
なわち、1」1工1a”工、である。FRの大き表ポリ
エチレンはど分子量分布が広く、流動性が優れている傾
向を示すが、PRが15を超すと、得られるフィルムの
透明性が低下するため本発明の方法では使用できない。
In addition, the flow ratio (hereinafter abbreviated as F) is JI8
In the K67600 melt index (hereinafter abbreviated as MI) measurement method, the value obtained using a load (Mllo) of 1a81g#) is the value obtained using a normal 2.16 wheel load (MI). The quotient obtained by dividing the In other words, it is 1"1a". FR large surface polyethylene has a wide molecular weight distribution and tends to have excellent fluidity, but when PR exceeds 15, the transparency of the resulting film decreases. It cannot be used in the method of the present invention because of this.

本発−で用いるポリプロピレン及びポリエチレンは、ポ
リエチレンのMIとポリプロピレンのメルトフローレー
ト(以下紐1と略称する)の比が12以上、すなわち、
MI/MIFR≧12で69、かつ、その晶合比が、ポ
リプロピレフ96〜85重量−、ポリエチレン4〜15
sの範回でなければならない、MIとMFfLの比がt
2に達L!いとフィルムのaEjA性が低下し好ましく
ない、ポリエチレンの混合率が4s未満では剛性向上の
効果が不足し、15チを超えるとフィルムが脆く、かつ
、遥@性の低下か大きくいずれも好ましくない、なお、
本J1@において組1とは、JIJli K675B 
(ポリブーピレン試験方法)に基いて固定しだものであ
る。
The polypropylene and polyethylene used in this invention have a ratio of MI of polyethylene to melt flow rate of polypropylene (hereinafter referred to as string 1) of 12 or more, that is,
MI/MIFR≧12 and 69, and the crystallization ratio is polypropylene 96 to 85 weight-, polyethylene 4 to 15
The ratio of MI and MFfL must be in the range of s.
Reached 2L! If the mixing ratio of polyethylene is less than 4s, the effect of improving the rigidity is insufficient, and if it exceeds 15s, the film becomes brittle and the properties are greatly reduced, both of which are undesirable. In addition,
In this J1@, group 1 is JIJli K675B
(Polybupylene test method).

本JA@で用いられる上記のポリプロピレン及びポリエ
チレンから成る組成物には、必要に応じポリオレフィン
用に通常に用いられる安定剤、加工助剤、帯電防止剤、
離燃剤、充填剤畳の他エチレンープロピレンゴム、エチ
レン酢酸ビニル共重合体等の偽の重合体等を本発明の目
的を損なわない範回で添加することが可−で番る。
The composition comprising the above polypropylene and polyethylene used in this JA@ contains stabilizers, processing aids, antistatic agents, etc. commonly used for polyolefins, as necessary.
In addition to flame release agents and fillers, false polymers such as ethylene-propylene rubber and ethylene-vinyl acetate copolymers may be added within limits that do not impair the purpose of the present invention.

上記組成物を用いてフィルムを成廖する方法として社、
公知のTダイ法チューブ2−法のいずれもが用いられる
が、押出機及びダイにおいて180〜250CでS融押
出された組成物が50℃以下に急冷されるような条件下
で製膜されねばならない。溶融押出の温度が180Cに
達し表いとフィルムの透明性が劣り、250℃を越すと
ポリエチレンのゲル化によるフィッシュアイが多脅し、
かつ、両樹脂のf&動性の差によりフィルム威彫性が不
安定とな9いずれも好ましくない、また溶融押出後の冷
却温度は50℃以下、好ましくは40C以下でme、s
o℃を超すとポリエチレンの結晶化によりフィルムが白
濁し、着るしく透明性が低下し、かつ、74身ムが脆く
なるので好ましくない。
As a method for growing a film using the above composition,
Any of the known T-die and tube methods can be used, but the film must be formed under conditions such that the composition is S-melt extruded at 180 to 250C in an extruder and die and is rapidly cooled to 50C or less. No. When the temperature of melt extrusion reaches 180C, the transparency of the surface and film deteriorates, and when it exceeds 250C, there is a risk of fish eyes due to gelation of polyethylene.
In addition, the film engraving properties are unstable due to the difference in f and dynamics between both resins.9 Both are unfavorable, and the cooling temperature after melt extrusion is 50°C or lower, preferably 40°C or lower.
If the temperature exceeds 0.degree. C., the film becomes cloudy due to crystallization of the polyethylene, the transparency becomes less comfortable to wear, and the film becomes brittle, which is not preferable.

本発明の方法によって得られるフィルムは、透明性、低
温ヒートシール性、高速ヒートシール!kに優れ、かつ
、従来公知のフイkAK比して格R#c優れた剛性を有
するため、単体フィルムや積層フィルムとして包義用を
主体として広い用辿を有するだけでなく、従来の同一用
途向けのフィルムに比して20〜5〇−程度厚みを簿(
で暑るので省資源の観点からも極めて有用である。
The film obtained by the method of the present invention has transparency, low-temperature heat-sealability, and high-speed heat-sealability! It has excellent rigidity and R#c compared to the conventionally known film AK, so it not only has a wide range of uses mainly for wrapping purposes as a single film or a laminated film, but also for the same conventional use. The thickness is about 20 to 50 mm compared to the film for
This is extremely useful from the perspective of resource conservation as it gets very hot.

以下本発明を実施例によって具体的に説明する。2&お
、実施flにおいて用いられたフィルム4I性の測定法
及び判定法を下記に示す。
The present invention will be explained in detail below using examples. 2&O, the method for measuring and determining the film 4I property used in the experiment fl is shown below.

(1)alllk : A8TMD1001 Kよる濁
度、−・(動剛性: A8TMD882 Kよるヤング
率(1チモジエツス) 、 kg/m μ)ヒートシーJ/a、シール強度500f/15■の
得られるシール温度、C シール条件:東洋精機製熱傾斜式シー に温度測定機、シール圧 力1v−・G、 1秒間 引張試験;試料片幅15 M 、引張速度60011I
/sII 得られるロールの表面の 平Jil性、巻きしわ、ロー ル端部の肥厚等を観察し た。
(1) alllk: Turbidity according to A8TMD1001 K, - (dynamic stiffness: Young's modulus (1 thymogietes) according to A8TMD882 K, kg/m μ) Heat sea J/a, sealing temperature at which a seal strength of 500f/15■ is obtained, C Sealing conditions: Toyo Seiki thermo-inclined seam with temperature measuring device, sealing pressure 1V-G, 1 second tensile test; sample width 15M, tensile speed 60011I
/sII The flatness of the surface of the obtained roll, the winding wrinkles, the thickening of the roll end, etc. were observed.

(6)フィッシュアイニー安用電機製作所at’フィッ
シュアイカウンター TPLSil ’を用い、直径0.1 −以上のフィッシュアイの 1000m?当たりの個数を 測定した。
(6) Fish eye with a diameter of 0.1 - or more using Fish Eye Electric Manufacturing Co., Ltd.' Fish Eye Counter TPLSil' for 1000 m? The number of hits was measured.

実施例1〜8.比較例1〜10 各種のグロビレンーα−オレフィン共重合体(フェノー
ル系酸化防止剤α1チ、ステアリン酸カルシウム[1,
1嘔、エルカ酸アミド(11慢を含有する)と各樵ポリ
エチレン(フエノー−S酸化防止剤cti s、ステア
リン酸カルシウムして、溶融押出温度220c、冷却ロ
ール温度50℃の条件でTダイ法による厚さ30#、幅
500鱈のフィルムを製膜し、それぞれ1000震を紙
管に巻き取った。得られたフィルムの特性およびフィル
ムの巻き姿を第1表に併記した。
Examples 1-8. Comparative Examples 1 to 10 Various globylene-α-olefin copolymers (phenolic antioxidant α1, calcium stearate [1,
1. Erucic acid amide (containing 11%) and polyethylene (phenol-S antioxidant CTIS, calcium stearate) were added to the thickness by T-die method under the conditions of melt extrusion temperature 220C and cooling roll temperature 50C. A film having a size of 30# and a width of 500 mm was formed, and 1000 rolls of each film were wound onto a paper tube.The characteristics of the obtained film and the form of the film are also listed in Table 1.

纂1表の結果から以下のことが明らかである。The following is clear from the results in Table 1.

(1) 211ピレン−α−オレフィン共141 体f
) Twaが低くなると、ヒートシール性は向上すゐが
剛性が著るしく低下しフィルムの巻き炎が不良となる。
(1) 211pyrene-α-olefin co-141 body f
) When Twa becomes low, the heat sealability improves, but the rigidity decreases significantly and the film winding flame becomes poor.

(a)本発明で限定された条件で製造されたフィルム(
実施例1〜8)は、透明性、剛性、衝撃強度、ヒートシ
ール性及びフィルムの轡自姿のいずれの特性も優れたも
のであるが、本発明の限定範閣外のフィルム(比較例1
〜10)は上記特性のうち少くとも1項目に欠点を有す
るものであ〕実用上好ましくない。
(a) Film manufactured under conditions limited in the present invention (
Examples 1 to 8) have excellent properties in terms of transparency, rigidity, impact strength, heat sealability, and film shape; however, the films outside the scope of the present invention (Comparative Example 1)
Items 1 to 10) have a defect in at least one of the above properties and are not preferred in practice.

実施例9〜16.比@1111〜15 エチレン含量2.811.1テン−1含量五3−#Tm
144℃、MFR7,口のエチレン−プロピレン−ブテ
ン−1三元共重合体くフェノール系酸化防止剤(119
6,ステアリン酸カルシウムa1−。
Examples 9-16. Ratio @1111~15 Ethylene content 2.811.1 Ten-1 content 53-#Tm
144°C, MFR7, ethylene-propylene-butene-1 terpolymer and phenolic antioxidant (119
6, calcium stearate a1-.

エルカ酸アミドa1−、シリカQ、1−を含有する)9
S −に% 密度Q、96Q  、  MI  111
0 、  li’Rs!0の高書度ポリエチレン(フェ
ノール系酸化防止剤α1s、ステアリン酸カルシウム0
.1LIIIを含有する)711を配合した組成物を用
い成膜条件(溶融押出温度及び冷却ロール温度)を種々
変更してTダイ法によシ厚さ25μ、@!400簡のフ
ィルムを得た。製膜条件及び得られたフィルムの特性を
第2表に示した。
Containing erucic acid amide a1-, silica Q, 1-)9
S-% Density Q, 96Q, MI 111
0, li'Rs! 0 high-density polyethylene (phenolic antioxidant α1S, calcium stearate 0
.. Using a composition containing 711 (containing 1LIII) and changing various film forming conditions (melt extrusion temperature and cooling roll temperature), the T-die method was used to form a film with a thickness of 25 μm, @! 400 pieces of film were obtained. Table 2 shows the film forming conditions and the properties of the obtained film.

jI2表の結果から、本発明の方法によって特性の優れ
たフィルムが得られることが明らかである。
From the results in Table jI2, it is clear that the method of the present invention provides a film with excellent properties.

112表 本1中やサージングあり 本2サージング大 以上112 tables There is surging in book 1 Book 2 surging large that's all

Claims (1)

【特許請求の範囲】[Claims] ぽリプ關ピレンが、結晶融点150 C以下、プロピレ
ン成分を70チ以上含有する結晶性ブーピレンーα−オ
レフィン共重合体で番食、ポリエチレンが、11度α9
45以上、7メCジオが15以下の高書度ポリエチレン
で番)、かつ、該ポリエチレンのメ身トインデレクス(
MI )と該ポリプルピレンのメ身トフローレー) (
MFR)の比が(MI741FR)≧t2であるような
ポ菅グーピレン!6〜85重量−とポリエチレン4〜1
5重量−とから威る龜威物を、180〜250℃でSS
押出し、50℃以下に菖檜することを轡黴とする透明性
及び剛性に優れた1ヒートシール性ポリオレアインフイ
身ムの製造方法。
Polypropylene is a crystalline boopylene-α-olefin copolymer with a crystal melting point of 150 C or less and a propylene component of 70 or more.
45 or more and 7 dimensional polyethylene of 15 or less), and the polyethylene's Meme Toindex (
(MI) and the polypropylene (MI)
MFR) ratio is (MI741FR)≧t2! 6-85 weight- and polyethylene 4-1
5 weight - SS at 180-250℃
1. A method for producing a heat-sealable polyolea film having excellent transparency and rigidity, which involves extrusion and heating at 50° C. or lower.
JP56105968A 1981-07-07 1981-07-07 Manufacture of polyolefin film Granted JPS587329A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56105968A JPS587329A (en) 1981-07-07 1981-07-07 Manufacture of polyolefin film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56105968A JPS587329A (en) 1981-07-07 1981-07-07 Manufacture of polyolefin film

Publications (2)

Publication Number Publication Date
JPS587329A true JPS587329A (en) 1983-01-17
JPS6140176B2 JPS6140176B2 (en) 1986-09-08

Family

ID=14421575

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56105968A Granted JPS587329A (en) 1981-07-07 1981-07-07 Manufacture of polyolefin film

Country Status (1)

Country Link
JP (1) JPS587329A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6052648A (en) * 1983-08-29 1985-03-25 昭和電工株式会社 Packing cloth
JPS61108649A (en) * 1984-11-02 1986-05-27 Idemitsu Petrochem Co Ltd Polyolefin resin composition
JPS61179248A (en) * 1985-02-04 1986-08-11 Idemitsu Petrochem Co Ltd Polyolefin resin composition
KR20000061149A (en) * 1999-03-24 2000-10-16 이영일 A thermoplastic resin composition
US6440577B1 (en) * 1998-06-01 2002-08-27 Basell Poliolefine Italia S.P.A. Propylene polymers suitable for transparent cast film
JP2002361809A (en) * 2001-06-04 2002-12-18 Japan Polychem Corp Packaging multilayered film
DE19983137B4 (en) * 1998-04-24 2009-04-02 Chisso Corp. Flame retardant polyolefin composition

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6052648A (en) * 1983-08-29 1985-03-25 昭和電工株式会社 Packing cloth
JPS61108649A (en) * 1984-11-02 1986-05-27 Idemitsu Petrochem Co Ltd Polyolefin resin composition
JPH0564180B2 (en) * 1984-11-02 1993-09-14 Idemitsu Petrochemical Co
JPS61179248A (en) * 1985-02-04 1986-08-11 Idemitsu Petrochem Co Ltd Polyolefin resin composition
JPH0136853B2 (en) * 1985-02-04 1989-08-02 Idemitsu Petrochemical Co
DE19983137B4 (en) * 1998-04-24 2009-04-02 Chisso Corp. Flame retardant polyolefin composition
US6440577B1 (en) * 1998-06-01 2002-08-27 Basell Poliolefine Italia S.P.A. Propylene polymers suitable for transparent cast film
KR20000061149A (en) * 1999-03-24 2000-10-16 이영일 A thermoplastic resin composition
JP2002361809A (en) * 2001-06-04 2002-12-18 Japan Polychem Corp Packaging multilayered film
JP4724316B2 (en) * 2001-06-04 2011-07-13 日本ポリプロ株式会社 Multilayer film for packaging

Also Published As

Publication number Publication date
JPS6140176B2 (en) 1986-09-08

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