JPS60228124A - Manufacture of laminated and oriented film - Google Patents

Manufacture of laminated and oriented film

Info

Publication number
JPS60228124A
JPS60228124A JP8570084A JP8570084A JPS60228124A JP S60228124 A JPS60228124 A JP S60228124A JP 8570084 A JP8570084 A JP 8570084A JP 8570084 A JP8570084 A JP 8570084A JP S60228124 A JPS60228124 A JP S60228124A
Authority
JP
Japan
Prior art keywords
film
laminated
polypropylene
stretching
stretched
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
Application number
JP8570084A
Other languages
Japanese (ja)
Inventor
Junkichi Watanabe
渡辺 純吉
Kenji Tsubouchi
健二 坪内
Shunichi Kawakita
川北 俊一
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP8570084A priority Critical patent/JPS60228124A/en
Publication of JPS60228124A publication Critical patent/JPS60228124A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • 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
    • B29C55/023Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets using multilayered plates or sheets
    • B29C55/026Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets using multilayered plates or sheets of preformed plates or sheets coated with a solution, a dispersion or a melt of thermoplastic material
    • 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
    • B29C55/10Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
    • B29C55/16Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial simultaneously
    • 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
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/08Copolymers of ethylene
    • B29K2023/083EVA, i.e. ethylene vinyl acetate copolymer
    • 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
    • B29K2023/10Polymers of propylene
    • B29K2023/12PP, i.e. polypropylene

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Laminated Bodies (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To obtain the titled film whose gas barrier properties are favorable, by making biaxial orientation of an unoriented and laminated film at a time, which is constituted with a saponified article of a polypropylene/ethylene-vinyl acetate copolymer laminated through coextrusion method. CONSTITUTION:After aqueous latex or a solvent solution of (B) polyvinylidene chloride series has been applied to at least one side of an unoriented and laminated film constituted with a saponified article of a polypropylene ethylene- vinyl acetate copolymer laminated through a (A) coextrusion method, an aimed film is obtained by making biaxial orientation of the laminated film at a time. As for percent of stretch, moreover, 3-3.5 times in a longitudinal direction and 3-4 times in a lateral direction are suitable for the titled film.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はポリプロピレンフィルムとエチレン酢酸ビニル
共重合体ケン化物(以下EVOHという)フィルムの積
層二軸延伸フィルムに関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a laminated biaxially stretched film of a polypropylene film and a saponified ethylene vinyl acetate copolymer (hereinafter referred to as EVOH) film.

EVOHフィルムは成型が比較的容易であり、しかもポ
リビニルアルコール系フィルムの中では耐湿性もある程
度改良されており、しかもその本来のガスバリヤ−性は
失われていないため食品包装用フィルムとしての優れた
適性を持つ素材である。
EVOH film is relatively easy to mold, and its moisture resistance has been improved to some extent among polyvinyl alcohol films, and its original gas barrier properties have not been lost, making it highly suitable as a food packaging film. It is a material that has

(従来の技術) しかしながらEVOHフィルムは高湿度条件ではその吸
水性のため、構造が緩和してガスバリヤ−性が低下する
という欠点は残る。特に耐熱性と低湿度条件下でのガス
バリヤ−性を維持するため、エチレン成分を少な(した
共重合組成物でこの傾向は強くなる。EVOHフィルム
を二軸延伸することによりこれらの欠点はある程度は改
良されるが1条件の厳しい用途分野では十分なバリヤー
材とはなりにくい。
(Prior Art) However, the EVOH film remains disadvantageous in that under high humidity conditions, its structure relaxes and its gas barrier properties deteriorate due to its water absorption properties. In particular, this tendency becomes stronger in copolymer compositions containing less ethylene component in order to maintain heat resistance and gas barrier properties under low humidity conditions.By biaxially stretching the EVOH film, these drawbacks can be overcome to some extent. Although improved, it is unlikely to be a sufficient barrier material in application fields with severe conditions.

又、延伸されたEVOHフィルムは屈曲強度が弱くこれ
は包装用フィルムとして重大な欠点となる。
Further, the stretched EVOH film has low bending strength, which is a serious drawback as a packaging film.

(発明が解決しようとする問題点) 本発明者等はEVOI(フィルムの持つ優れた素質を生
かし1しかも上記した欠点をカッ\−したフィルムを経
済的に製造する方法について鋭意研究した結果本発明方
法に到達した。
(Problems to be Solved by the Invention) The inventors of the present invention have conducted intensive research on a method for economically manufacturing EVOI (films that take advantage of their excellent qualities and eliminate the above-mentioned drawbacks), and have invented the present invention. reached the method.

すなわちCVOHフィルムの耐湿性、耐屈曲ピンホール
性をカバーするためには、二軸延伸ポリプロピレンフィ
ルムを積層し、しかも両者を共押出法で積層しこれを共
延伸することにより後加工でポリプロピレンフィルムを
ラミネートするよりはるかに低コストで積層フィルムを
製造する方法である。
In other words, in order to cover the moisture resistance and bending pinhole resistance of CVOH film, biaxially oriented polypropylene films are laminated, and both are laminated by co-extrusion and co-stretched, thereby making it possible to create a polypropylene film in post-processing. This is a method of producing laminated films at a much lower cost than laminating.

単体フィルムで延伸する場合、ポリプロピレンフィルム
とEVOHフィルムとでは最適延伸倍率は大中に異なる
。ポリプロピレンフィルムは縦横方向ともそれぞれ5倍
以上に延伸されるのが一般であり、5倍以下では均一延
伸されない。一方c v o uフィルムの延伸倍率は
一般的な共重合組成物の場合。
When stretching a single film, the optimum stretching ratio is quite different between a polypropylene film and an EVOH film. Generally, a polypropylene film is stretched five times or more in both the longitudinal and transverse directions, and cannot be stretched uniformly if it is less than five times. On the other hand, the stretching ratio of the cvou film is that of a general copolymer composition.

縦横とも3倍程度である。しかしながら本発明者等は両
者を共押出法で積層し、これを同時二軸延伸法で共延伸
する場合は接着剤の選定を考慮することによりEVOl
lの延伸倍率すなわち縦横それぞれ3倍程度の延伸倍率
でもポリプロピレンは均一延伸され、しかも実用上十分
な配向効果の得られることを知った。これはEVOHの
延伸応力が大きいため延伸変形挙動はEVO)Iが支配
し、ポリプロピレンはEVOllの変形に従って均一延
伸されるからである。
It is about three times as large both in length and width. However, the present inventors have found that when they are laminated by a coextrusion method and then co-stretched by a simultaneous biaxial stretching method, by considering the selection of the adhesive, the EVO
It has been found that polypropylene can be uniformly stretched even at a stretching ratio of 1, that is, a stretching ratio of about 3 times in both the length and width, and that a practically sufficient orientation effect can be obtained. This is because the stretching stress of EVOH is large, so the stretching deformation behavior is dominated by EVO)I, and polypropylene is uniformly stretched according to the deformation of EVOll.

なおこれは同時二軸延伸法でのみ可能な方法であり、二
段二軸延伸法ではまずEVOIIの延伸が困難であり、
又EVO)I中のエチレン成分を増して延伸性を改良し
ても延伸時に発生する接着面の剪断応力により両者が剥
離する。
Note that this is only possible with the simultaneous biaxial stretching method, and it is difficult to stretch EVOII with the two-stage biaxial stretching method.
Furthermore, even if the ethylene component in EVO)I is increased to improve the stretchability, the two will peel off due to the shear stress generated on the adhesive surface during stretching.

(問題点を解決するための手段) 本発明の構成要素であるEVOllとはエチレン含有率
が25〜50モル%でケン化度98%以上のものである
。エチレン含有率が低いものほど品質上からはバリヤー
性、耐熱性の優れた積層延伸フィルムが得られるがポリ
プロピレンとの共延伸性が低下する。逆にエチレン含有
率が大きくなりすぎると品質上でバリヤー性が低下し、
又延伸応力が低下して均一延伸が難しくなる。
(Means for Solving the Problems) EVOll, which is a component of the present invention, has an ethylene content of 25 to 50 mol% and a saponification degree of 98% or more. The lower the ethylene content, the better the quality of the laminated stretched film in terms of barrier properties and heat resistance, but the lower the co-stretchability with polypropylene. On the other hand, if the ethylene content becomes too high, the quality of the barrier properties will decrease,
Furthermore, the stretching stress decreases, making uniform stretching difficult.

本発明方法で用いるポリプロピレンとはポリプロピレン
ホモポリマー又はポリプロピレンホモポリマーを80%
以上含有して、他のα−オレフィン類等と共重合された
ものであり、滑剤、帯電防止剤等の添加剤を含有したも
のを含む。
The polypropylene used in the method of the present invention is polypropylene homopolymer or 80% polypropylene homopolymer.
These are copolymerized with other α-olefins, etc., and include those containing additives such as lubricants and antistatic agents.

ポリプロピレン/EVO11の積層フィルムの片面又は
両面にポリ塩化ビニリデン(以下PVDCという)層を
設けることにより本発明方法により得られるフィルムの
バリヤー性能はさらに改良される。この場合もPVDC
は延伸前に積層し、共延伸により配向効果を与えること
によりPVDCのバリヤー性能は改良される。ここにp
vocとはポリ塩化ビニリデンの基本的性能を変えない
範囲で塩化ビニル、アクリコニ1リル、アクリル酸エス
テル等が共重合されたものであり、これらのPVDCは
水性ラテックス。
By providing a polyvinylidene chloride (hereinafter referred to as PVDC) layer on one or both sides of the polypropylene/EVO11 laminated film, the barrier performance of the film obtained by the method of the invention is further improved. In this case as well, PVDC
The barrier performance of PVDC is improved by laminating them before stretching and co-stretching to provide an orientation effect. p here
VOC is a copolymer of vinyl chloride, acrylonilyl, acrylic ester, etc. without changing the basic performance of polyvinylidene chloride, and these PVDCs are water-based latex.

溶媒溶液として塗布される。ポリ塩化ビニリデン成分が
多いほどバリヤー性能は優れるがラテックス、溶液のボ
ットライフが短くなりすぎたり、均一塗布性が低下する
Applied as a solvent solution. The higher the polyvinylidene chloride component, the better the barrier performance, but the bottling life of the latex or solution becomes too short and the uniformity of application decreases.

ポリプロピレンとE V O11フイルムの厚さ比率は
2:8〜6:4の範囲が適しており、用途上の目的に応
して最適の構成比率を決定する。片面又は両面にpvo
cmを設ける場合、 PVDC層の厚みは延伸。
The thickness ratio of polypropylene and E V O11 film is suitably in the range of 2:8 to 6:4, and the optimum composition ratio is determined depending on the purpose of use. PVO on one or both sides
cm, the thickness of the PVDC layer is stretched.

結晶化後で0.5〜2μの範囲が通している。After crystallization, a range of 0.5 to 2μ is passed.

又積層フィルムの全厚は延伸後で15〜30μの範囲で
本発明の効果が最も顕著に発現する。
Further, the effects of the present invention are most clearly exhibited when the total thickness of the laminated film is in the range of 15 to 30 μm after stretching.

(作用) 次に本発明方法の作用について説明する。(effect) Next, the operation of the method of the present invention will be explained.

ポリプロピレンとEVO)Iフィルムの積層は基本的に
は3台の押出機と3層Tダイの組み合わされた共押出装
置を用いて行う。ここに3番目の押出機にはポリプロピ
レン層とEVOH層の間に流し込む接着性樹脂のための
ものであり、接着性樹脂としては一般的には変性ポリオ
レフィン樹脂を用いるが。
Lamination of polypropylene and EVO)I film is basically carried out using a coextrusion device that is a combination of three extruders and a three-layer T-die. The third extruder is for adhesive resin poured between the polypropylene layer and the EVOH layer, and modified polyolefin resin is generally used as the adhesive resin.

二軸延伸工程で界面に剪断力が作用して接着性を阻害す
ることがあるため、接着性樹脂の種類と層厚みの選定に
は十分な注意が必要である。接着強度が特に要求される
場合は架橋性接着剤を用いることが望ましい場合もある
Since shearing force acts on the interface during the biaxial stretching process and may impair adhesion, sufficient care must be taken in selecting the type of adhesive resin and the layer thickness. It may be desirable to use a crosslinkable adhesive if particular adhesive strength is required.

ポリプロピレン/ EVOI+積層フィルムの片面又は
両面にさらにpvoc層を設ける場合は、共押出法で得
たポリプロピレン/F、VOII積層無配向フィルムの
片面又両面にPVDC水性ラテックス又は溶剤溶液を塗
布し、少なくとも塗布面の粘着性がなくなる程度まで乾
燥した後延伸機に繰込む。塗布はエアーナイフ法、グラ
ビアロール法、リバースロール法。
When providing an additional pvoc layer on one or both sides of the polypropylene/EVOI+ laminated film, coat one or both sides of the polypropylene/F, VOII laminated non-oriented film obtained by coextrusion with a PVDC aqueous latex or solvent solution, and at least apply After drying until the surface is no longer sticky, it is fed into a stretching machine. Application is done by air knife method, gravure roll method, and reverse roll method.

バーコード法等で行い乾燥はアーチ式、フローティング
式等の乾燥炉で行う。延伸前にpvocを塗布し、しか
る後に延伸することの第一の目的はpvoc層も二輪配
向してバリヤー性能を高めることであるが、それ以外の
効果としてこの方法によりアンカー処理を行うことなし
にEVO)I/ PVDC間、ポリプロピレン/PνD
C間の接着性が向上することが判った。この理由は本発
明者にも明らかでないが延伸後に行う高温熱処理の効果
が関係していると考えられる。又pvoc水性ラテック
スをEVOI−1面に塗布する場合は塗布液中の水分が
EVOI中に移行してEVOI(を可塑化し、 EVO
I+の延伸性を高めるという効果が認められる。
Drying is performed using a bar code method, etc., and drying is performed in an arch type, floating type, etc. drying oven. The primary purpose of applying PVOC before stretching and then stretching is to also orient the PVO layer to improve barrier performance, but the other effect is that this method can be used without anchoring. EVO) I/PVDC, polypropylene/PνD
It was found that the adhesion between C was improved. The reason for this is not clear even to the inventors, but it is thought that it is related to the effect of the high temperature heat treatment performed after stretching. In addition, when applying PVOC water-based latex to the EVOI-1 surface, the water in the coating liquid migrates into the EVOI and plasticizes the EVOI.
The effect of increasing the stretchability of I+ is recognized.

ポリプロピレン/ EVOH構成の無配向積層フィルム
又はこれにPVDCを塗布したフィルムは同時二軸延伸
機に繰込んで延伸する。
A non-oriented laminated film having a polypropylene/EVOH structure or a film coated with PVDC is fed into a simultaneous biaxial stretching machine and stretched.

同時二軸延伸機とは無配向フィルムの両端を無端リンク
チェーンにとりつけられたクリップで把持し、クリップ
が平行に進行する予熱ゾーンで延伸温度まで加熱され7
次の延伸ゾーンでは相対するクリップ間距離が末広がり
的に拡大することにより横方向に延伸され、同時に流れ
方向のクリップ間ピンチが漸次大きくなりクリップ進行
速度が増大することにより縦方向に延伸される。延伸ゾ
ーンの次にはクリップが平行、一定速度で走行し高温の
熱風が吹きつけられる熱処理ゾーンが設けられており、
ここで延伸フィルムの熱セットが行われる。
A simultaneous biaxial stretching machine is a machine in which both ends of an unoriented film are held by clips attached to an endless link chain, and the clips are heated to the stretching temperature in a preheating zone where they advance in parallel.
In the next stretching zone, the distance between the opposing clips widens in a divergent manner, resulting in stretching in the transverse direction, and at the same time, the pinch between the clips in the machine direction gradually increases, increasing the speed of clip advancement, resulting in stretching in the longitudinal direction. Next to the stretching zone is a heat treatment zone where the clips run in parallel at a constant speed and are blown with high temperature hot air.
Here, the stretched film is heat set.

延伸倍率は縦方向3〜3.5倍、横方向3〜4倍か適し
ており、延伸温度は90〜150℃の範囲から選ぶ。熱
処理温度はポリプロピレンの融点とEVOI+の融点の
うち低い方の温度以下で行う必要がある。
The stretching ratio is suitably 3 to 3.5 times in the longitudinal direction and 3 to 4 times in the transverse direction, and the stretching temperature is selected from the range of 90 to 150°C. The heat treatment temperature must be lower than the lower of the melting point of polypropylene and the melting point of EVOI+.

次に実施例により本発明方法を具体的に説明する。Next, the method of the present invention will be specifically explained with reference to Examples.

(実施例) 実施例L2,3および比較例 ポリプロピレン、エチレン含量30モル%のEVOIL
カルボン酸変性ポリオレフィン系接着剤を3台の押出機
で溶融し、マルチマニホールド型3層グイで押出し冷却
ロールで急冷する方法で、厚み構成の異なる3種類の無
配向積層フィルムを得た。得られたフィルムを同時二軸
延伸機に繰込み縦方向3.0倍、横方向3.3倍に同時
二輪延伸して3種類の積層延伸フィルムを得た。得られ
たフィルムの厚み構成(接着剤層の厚みは0.5〜1μ
)と物性値を同し原料EνOHで製造したE V O1
1単体フィルムと比較して表に示す。
(Example) Examples L2 and 3 and Comparative Example Polypropylene, EVOIL with ethylene content of 30 mol%
Three types of non-oriented laminated films with different thickness configurations were obtained by melting a carboxylic acid-modified polyolefin adhesive using three extruders, extruding it using a multi-manifold type three-layer gouer, and rapidly cooling it using a cooling roll. The obtained film was fed into a simultaneous biaxial stretching machine and stretched simultaneously on two wheels to 3.0 times in the longitudinal direction and 3.3 times in the transverse direction to obtain three types of laminated stretched films. Thickness structure of the obtained film (the thickness of the adhesive layer is 0.5 to 1 μm)
) E V O1 manufactured from raw material EνOH with the same physical properties as
A comparison with 1 single film is shown in the table.

1” に 表より明らかな如く本発明フィルムは[!VOI+フィ
ルムの酸素ガスバリヤ−性をそれほど失うことなく耐屈
曲性が大巾に改良される。
As is clear from the table in Table 1, the film of the present invention has greatly improved bending resistance without significantly losing the oxygen gas barrier properties of the VOI+ film.

実施例4 実施例1と同じ方法でポリプロピレン/EVO11積層
無配向フィルムを製造した後、 EVOI面に塩化ビニ
リデン成分を92重量%含むPVDC水性ラテックスを
延伸後で1.5μのPVDC層が形成されるように塗布
乾燥し、しかる後に実施例1と同じ方法で同時二軸延伸
した。得られたフィルムの酸素ガス透過量(cc/ r
d ・24hr)は65%I’lllで0.5以下さら
に100%R11でも2.0以下であり水蒸気透過量(
g/r+(・24hr)は3.0以下の極めて優れたも
のであった。
Example 4 After manufacturing a polypropylene/EVO11 laminated non-oriented film in the same manner as in Example 1, a PVDC aqueous latex containing 92% by weight of vinylidene chloride component was stretched on the EVOI surface to form a 1.5μ PVDC layer. The film was coated and dried as described above, and then simultaneously biaxially stretched in the same manner as in Example 1. Oxygen gas permeation rate (cc/r) of the obtained film
d・24hr) is less than 0.5 at 65% I'll, and is less than 2.0 even at 100% R11, and the amount of water vapor permeation (
g/r+(·24hr) was 3.0 or less, which was extremely excellent.

(発明の効果) 熱処理後のフィルムは両耳部をトリミングした後巻取ら
れて製品となるが、トリミング耳部分はEVOI(単体
とすることにより容易にリサイクルが行い得る。二軸延
伸した積層フィルムは必要に応してコロナ処理、Uv前
照射エージング等の後処理をされる。かくして得られた
積層延伸フィルムは印刷、さらにンーラントとラミネー
トするなどして包装材料となる。
(Effect of the invention) The heat-treated film is trimmed at both edges and then rolled up to become a product. The trimmed edges are EVOI (by making it a single unit, it can be easily recycled. A biaxially stretched laminated film. If necessary, the film is subjected to post-treatments such as corona treatment, pre-UV irradiation aging, etc. The laminated stretched film thus obtained is printed and further laminated with a wet film to become a packaging material.

本発明はバリヤー性能は優れるが耐湿性、耐屈曲ピンホ
ール性に欠点を持つEVOHフィルムにポリプロピレン
フィルムを積層してこれらの欠点をカハーシ、シかもそ
れを共押出、共延伸法という経済的な方法で実現したも
のであり、その工業的価値は極めて大きい。
In the present invention, a polypropylene film is laminated onto an EVOH film that has excellent barrier performance but has shortcomings in moisture resistance and bending pinhole resistance, and these shortcomings can be overcome using an economical method of co-extrusion and co-stretching. The industrial value of this technology is extremely large.

特許出願人 ユニチカ株式会社Patent applicant: Unitika Co., Ltd.

Claims (1)

【特許請求の範囲】 1、共押出法で積層したポリプロピレン/エチレン酢酸
ビニル共重合体ケン化物構成の無配向積層フィルムを同
時二輪延伸することを特徴とする積層延伸フィルムの製
造方法。 2、共押出法で積層したポリプロピレン/エチレン酢酸
ビニル共重合体ケン化物構成の無配向積層フィルムの少
なくとも片面にポリ塩化ビニリデン系樹脂の水性ラテッ
クス又は溶剤溶液を塗布した後、該積層フィルムを同時
二軸延伸することを特徴とする特許請求の範囲第1項記
載の製造方法。
[Claims] 1. A method for producing a laminated stretched film, which comprises simultaneous two-wheel stretching of an unoriented laminated film composed of a saponified polypropylene/ethylene-vinyl acetate copolymer laminated by a coextrusion method. 2. After coating an aqueous latex or solvent solution of polyvinylidene chloride resin on at least one side of a non-oriented laminated film composed of saponified polypropylene/ethylene vinyl acetate copolymer laminated by coextrusion method, the laminated film is simultaneously The manufacturing method according to claim 1, characterized in that axial stretching is carried out.
JP8570084A 1984-04-26 1984-04-26 Manufacture of laminated and oriented film Pending JPS60228124A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8570084A JPS60228124A (en) 1984-04-26 1984-04-26 Manufacture of laminated and oriented film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8570084A JPS60228124A (en) 1984-04-26 1984-04-26 Manufacture of laminated and oriented film

Publications (1)

Publication Number Publication Date
JPS60228124A true JPS60228124A (en) 1985-11-13

Family

ID=13866096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8570084A Pending JPS60228124A (en) 1984-04-26 1984-04-26 Manufacture of laminated and oriented film

Country Status (1)

Country Link
JP (1) JPS60228124A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52146487A (en) * 1976-06-01 1977-12-06 Mitsui Petrochem Ind Ltd Oriented, laminated films and their mnaufacture
JPS55133928A (en) * 1979-04-05 1980-10-18 Unitika Ltd Method for correcting curl of laminate film

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52146487A (en) * 1976-06-01 1977-12-06 Mitsui Petrochem Ind Ltd Oriented, laminated films and their mnaufacture
JPS55133928A (en) * 1979-04-05 1980-10-18 Unitika Ltd Method for correcting curl of laminate film

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