JPS6049910A - Manufacture of synthetic resin mono-layered film having property of thermoplastic polyester film - Google Patents

Manufacture of synthetic resin mono-layered film having property of thermoplastic polyester film

Info

Publication number
JPS6049910A
JPS6049910A JP58159219A JP15921983A JPS6049910A JP S6049910 A JPS6049910 A JP S6049910A JP 58159219 A JP58159219 A JP 58159219A JP 15921983 A JP15921983 A JP 15921983A JP S6049910 A JPS6049910 A JP S6049910A
Authority
JP
Japan
Prior art keywords
film
resin
ethylene
thermoplastic polyester
polyethylene
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
JP58159219A
Other languages
Japanese (ja)
Inventor
Jiyun Kiyosato
清里 潤
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.)
Dai Nippon Printing Co Ltd
Original Assignee
Dai Nippon Printing 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 Dai Nippon Printing Co Ltd filed Critical Dai Nippon Printing Co Ltd
Priority to JP58159219A priority Critical patent/JPS6049910A/en
Publication of JPS6049910A publication Critical patent/JPS6049910A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • 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
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0019Combinations of extrusion moulding with other shaping operations combined with shaping by flattening, folding or bending
    • 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
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • 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
    • B29K2067/00Use of polyesters or derivatives thereof, as moulding material

Landscapes

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

Abstract

PURPOSE:To easily and exactly obtain a mono-layered film by forming the film of a mixed resin composed of polyester and polyethylene in a specific proportion by an inflation method. CONSTITUTION:Raw material for forming a film is a mixed resin composed of 20-95wt% thermoplastic polyester resin and 80-5wt% polyethylene resin having polyethylene chains and containing 50wt% or more ethylene. The raw material is molded into a film by an inflation method in which the raw material is melted and extruded at about 140 deg.C through a circular die 2 of an extruder 1 into a film. The polyethylene resin can be easily pulled up in the form of a tubular film by pinch rolls 3 and 4 and rolled up by a roll 6 without damaging the characteristics of the polyester film obtained.

Description

【発明の詳細な説明】 性質を有する合成樹脂製単層フイルムの製造方法に関す
るものであり、被接着体との間の接着強度がコントロー
ルされている合成樹脂製工層フイルムを、インフレーシ
ョン法によるフィルム成形法にて容易,かつ確実に得る
方法を提供するものである。
[Detailed Description of the Invention] This relates to a method for producing a single layer film made of synthetic resin having the following properties: This provides a method for easily and reliably obtaining it using a molding method.

飽和多塩基酸と多価アルコールとの共重合によって得゛
られる熱可塑性ポリエステル樹脂のうちには、一旦溶融
すると再結晶寸でに非常に長時間を要するものが多く、
しかもこの間における成形品(フィルム)表面は粘着性
に富み、この熱可塑性ポリエステル樹脂成形品同士の場
合は勿論のこと、他の金属表面やプラスチックス表面等
に対しても粘着性を有するため熱可塑性ポリエステルの
単層フィルムを製造する場合には種々のトラブルが発生
していた。加えて、この熱可塑性ポリエステル樹脂は、
溶融時における張力及び粘度が小さいため、インフレー
ション法によって単層フィルムを得ることは殆んど不可
能であった。
Many of the thermoplastic polyester resins obtained by copolymerizing saturated polybasic acids and polyhydric alcohols require a very long time to recrystallize once melted.
Moreover, the surface of the molded product (film) during this period is highly adhesive, and it is adhesive not only to thermoplastic polyester resin molded products to each other, but also to other metal surfaces, plastic surfaces, etc. Various troubles have occurred when producing single-layer polyester films. In addition, this thermoplastic polyester resin
Due to the low tension and viscosity during melting, it was almost impossible to obtain a single layer film by the inflation method.

本発明は、製膜用原料中の合成樹脂成分を、熱可塑性ポ
リエステル樹脂20〜95重量%と、ポリエチレン鎖を
具備し、しかもエチレン含有率が50重量%以上のポリ
エチレン系樹脂80〜5重量%との混合樹脂で構成し、
この製膜用原料をインフレーション法によるフィルム成
形に付すことにより、本来の熱可塑性ポリエステル製フ
ィルムの具備する物理的性質を損うことのない合成樹脂
の単層フィルムを、安定した状態で効率良く得る方法を
提供し得たものである。
In the present invention, the synthetic resin components in the raw material for film forming are 20 to 95% by weight of a thermoplastic polyester resin and 80 to 5% by weight of a polyethylene resin having a polyethylene chain and having an ethylene content of 50% by weight or more. Consists of a mixed resin with
By subjecting this film-forming raw material to film forming using the inflation method, a single-layer synthetic resin film that does not impair the physical properties of the original thermoplastic polyester film can be efficiently obtained in a stable state. This method could have been provided.

本発明の熱可塑性ポリエステル製フィルムの性質を有す
る合成樹脂製単層フィルムの製造方法は、製膜用原料た
る合成樹脂成分が、飽和ポリエステル樹脂すなわち熱可
塑性ポリエステル樹脂20〜95重量%と、ポリエチレ
ン鎖を具備し、しかもエチレン含有率が5L重量%以上
のポリエチレン系樹脂80〜5重量%との混合樹脂によ
って構成されるもので、熱可塑性ポリエステル樹脂とし
ては、例えば、フタル酸,イノフタル酸,テレフタル酸
,マレイン酸,マレイン酸誘導体,コハク酸,アジピン
酸,セバシン酸等の飽和多塩基酸と、エチレングリコー
ル。
The method for producing a single-layer synthetic resin film having the properties of a thermoplastic polyester film according to the present invention is such that the synthetic resin component, which is a raw material for film formation, contains 20 to 95% by weight of a saturated polyester resin, that is, a thermoplastic polyester resin, and a polyethylene chain. It is composed of a mixed resin with 80 to 5% by weight of a polyethylene resin having an ethylene content of 5L% by weight or more, and examples of the thermoplastic polyester resin include phthalic acid, inophthalic acid, and terephthalic acid. , maleic acid, maleic acid derivatives, succinic acid, adipic acid, sebacic acid and other saturated polybasic acids, and ethylene glycol.

ジエチレングリコール,グリセリン,トリメチロールプ
ロパン, 1.2−プロピレングリコール。
Diethylene glycol, glycerin, trimethylolpropane, 1,2-propylene glycol.

1、3−ブタンジオール,ジプロピレングリコール,1
,4−ブタンジオール,1,6−ヘキサンジオール,ペ
ンタエリスリノト,ノルビト−ル。
1,3-butanediol, dipropylene glycol, 1
, 4-butanediol, 1,6-hexanediol, pentaerythrinote, norbitol.

ネオペンチルグリコール,1,4−シクロヘキサンジメ
タノール等の多価アルコールとのエステル結合によシ得
られるポリエステル樹脂が、またポリエチレン鎖を具備
し、しかもエチレン含有率が50重量%以上のポリエチ
レン系樹脂としては、例えば、高密度ポリエチレン,中
密度ポリエチレン,低密度ポリエチレン,エチレン−α
−オレフィン共重合体,エチレン−酢酸ビニル共重合体
,アイオノマー,エチレン−エチルアクリレート共重合
体,エチレンー酢酸ビニル共重合体ケン化物等のエチレ
ン重合体首だはエチレン共重合体あるいはこれらの混合
物等が利用される。
A polyester resin obtained by ester bonding with a polyhydric alcohol such as neopentyl glycol, 1,4-cyclohexanedimethanol, etc. also has a polyethylene chain and has an ethylene content of 50% by weight or more as a polyethylene resin. For example, high density polyethylene, medium density polyethylene, low density polyethylene, ethylene-α
- Ethylene polymers such as olefin copolymers, ethylene-vinyl acetate copolymers, ionomers, ethylene-ethyl acrylate copolymers, saponified ethylene-vinyl acetate copolymers, etc., ethylene copolymers, or mixtures thereof, etc. used.

前記製膜用原料たる合成樹脂成分中のポリエチレン系樹
脂は、得られるフィルムに具備される物理的性質が熱可
塑性ポリエステル樹脂によって得られるフィルムの性質
を損なうようなことがなく、シかも熱可塑性ポリエステ
ル樹脂の「一旦溶融すると再結晶までに非常に長時間を
要する」、「溶融から再結晶寸での間における成形品表
面が高粘着性である」、「溶融時における張力及び粘度
が低い」等の性質を改質するもので、ポリエチレン系樹
脂の配合量やその種類は、合成樹脂成分として利用され
るもう一方の成分である熱可塑性ポリエステル樹脂との
混線性、得られるフィルムに要求される物理的性質、使
用されるインフレーション式フィルム成形機の性能等を
勘案したうえで全樹脂成分中の80〜5重量%を占める
ように配合されるものである。これは、ポリエチレン系
樹脂の配合量が5M量%未満では、インフレーション法
によるフィルム成形時の熱可塑性ポリエステル樹脂の「
一旦溶融すると再結晶捷でに非常に長時間を要する」、
「溶融から再結晶までの間における成形品表面の粘着性
が高い」、「溶融時における低張力及び低粘度」等の改
質が十分でないこと、またポリエチレン系樹脂の配合量
が80重量%を超えると、得られる単層フィルムの性質
が熱可塑性ポリエステル樹脂フィルムの物理的性状から
かけ離れ、熱可塑性ポリエステル樹脂フィルム本来の性
質を具備する単層フィルムを得ることが出来なくなるだ
めである。
The polyethylene resin in the synthetic resin component, which is the raw material for film formation, does not impair the physical properties of the film obtained by the thermoplastic polyester resin, and is suitable for thermoplastic polyester resins. The resin "takes a very long time to recrystallize once melted", "the surface of the molded product is highly sticky between melting and recrystallization", "tension and viscosity during melting are low", etc. The amount of polyethylene resin blended and its type are determined based on the crosstalk with the thermoplastic polyester resin, which is the other component used as a synthetic resin component, and the physical properties required for the resulting film. It is blended in such a way that it accounts for 80 to 5% by weight of the total resin components, taking into consideration the physical properties and the performance of the inflation film forming machine used. This means that if the blending amount of polyethylene resin is less than 5M%, the thermoplastic polyester resin will be
Once melted, it takes a very long time to recrystallize.
Insufficient modifications such as "high adhesiveness on the surface of the molded product during the period from melting to recrystallization" and "low tension and low viscosity during melting", and that the amount of polyethylene resin blended is 80% by weight If it exceeds the range, the properties of the resulting single-layer film will be far different from the physical properties of the thermoplastic polyester resin film, and it will become impossible to obtain a single-layer film having the properties inherent to the thermoplastic polyester resin film.

以下、本発明の熱可塑性ポリエステル製フィルムの性質
を有する合成樹脂製単層フィルムの製造方法の具体的構
成を実施例に基いて説明する。
Hereinafter, the specific structure of the method for producing a single-layer synthetic resin film having the properties of the thermoplastic polyester film of the present invention will be explained based on Examples.

実施例 熱可塑性飽和ポリエステル樹脂〔バイロンGM−900
:東洋紡績(株)製、比重1.25 、融点113℃〕
50重量%と、低密度ポリエチレン〔ミラノン−16P
:三井ポリケミカル(株)製。
Examples Thermoplastic saturated polyester resin [Vylon GM-900
: Manufactured by Toyobo Co., Ltd., specific gravity 1.25, melting point 113℃]
50% by weight and low density polyethylene [Milanon-16P
: Manufactured by Mitsui Polychemical Co., Ltd.

密度0.917 、メルトインデックス3.7)5o重
量%との混合物を良くブレンドシフ、図面に示されるよ
う彦一般的なインフレーション法によるフィルム成形機
を使用し、押出機1から1.40℃で元型ダイ2を通じ
て溶融押出し、フィルム成形に付したところ、フィルム
成形状態は良好で、スリッター、口開きの各工程をイン
ラインで行っても全く問題なく巻取りロール6で巻取る
ことが出来た。
Density 0.917, melt index 3.7) 50% by weight and blend well, using Hiko's general inflation film forming machine as shown in the drawing, extruder 1 at 1.40 °C. When the film was melt-extruded through the master die 2 and subjected to film forming, the film was in good condition and could be wound up with the winding roll 6 without any problems even when the slitter and opening steps were carried out in-line.

尚、参考のために、飽和熱可塑性ポリエステル樹脂〔バ
イロンGM−900)を115〜140℃の範囲で溶融
押出し、フィルム成形を試みだが、樹脂の溶融時の張力
が小さく、チューブ状フィルムをピンチロール3,4ま
で引き上げることが困難であったばかりか、フィルム成
形工程中にあるフィルム5が、ピンチロール3たる金属
ロー/L[面及[ピンチロール4たるゴムロール表面に
強く粘着して巻き伺き、フィルム成形機の運転が不能と
なった。
For reference, we attempted to melt and extrude a saturated thermoplastic polyester resin (Vylon GM-900) at a temperature of 115 to 140°C to form a film, but the tension during melting of the resin was small, and the tubular film was pinch-rolled. Not only was it difficult to pull the film up to 3 and 4, but during the film forming process, the film 5 strongly adhered to the surface of the metal row/L (pinch roll 3) and the rubber roll (pinch roll 4). The film forming machine became unable to operate.

本発明は以上の説明の通り、エチレン含有率が50重量
%以上のポリエチレン系樹脂を改質剤として添加する熱
可塑性ポリエステル樹脂の単層フィルムをインフレーシ
ョン法ニよって得る合成樹脂製フィルムの製造方法、す
なわち、熱可塑性ポリエステル樹脂20〜95重量%と
、ポリエチレン鎖を具備し、しかもエチレン含有率が5
0i量%以上のポリエチレン系樹脂80〜5重量%との
混合樹脂を合成樹脂成分とする製膜用原料を、インフレ
ーション法によるフィルム成形に付す合成樹脂製単層フ
ィルムの製造方法からなるもので、ポリエチレン系樹脂
の添加が、得られる合成樹脂製単層フィルムにおける熱
可塑性ポリエステル製フィルムの本来の性質を損うこと
なく、しかも熱可塑性ポリエステル樹脂の有する「一旦
溶融すると再結晶1でに非常に長時間を要する」、「溶
融から再結晶までの間における成形品(フィルム)表面
が高粘着性である」、「溶融時における張力及び粘度が
低い」等のインフレーション式フィルム成形の際の欠点
を改質するので、熱可塑性ポリエステル製フィルムの性
質を有する合成樹脂製単層フィルムを、効率の良いイン
フレーション式にて、安定して得ることが出来るという
作用、効果を奏する。
As explained above, the present invention provides a method for producing a synthetic resin film in which a monolayer film of a thermoplastic polyester resin to which a polyethylene resin having an ethylene content of 50% by weight or more is added as a modifier is obtained by an inflation method; That is, it contains 20 to 95% by weight of thermoplastic polyester resin and polyethylene chains, and has an ethylene content of 5% by weight.
A method for producing a single layer film made of synthetic resin, in which a raw material for film forming, whose synthetic resin component is a mixed resin with 80 to 5% by weight of polyethylene resin of 0i% or more, is subjected to film forming by an inflation method, The addition of the polyethylene resin does not impair the original properties of the thermoplastic polyester film in the resulting synthetic resin single-layer film. We have improved the disadvantages of inflation film molding, such as "it takes a long time", "the surface of the molded product (film) is highly sticky between melting and recrystallization", and "low tension and viscosity during melting". As a result, it is possible to stably obtain a single-layer synthetic resin film having the properties of a thermoplastic polyester film using an efficient inflation method.

まだ、本発明の熱可塑性ポリエステル製フィルムの性質
を有する合成樹脂製単層フィルムの製造方法においては
、製膜用原料中のポリエチレン系樹脂の量が得られるフ
ィルムの表面粘着特性を左右するので、用途に応じて所
望される表面粘着力を具備する合成樹脂製フィルムを、
製膜用原料中の熱可塑性ポリエステル樹脂とポリエチレ
ン系樹脂との間の比率を変えることによって容易に得る
ことが出来るという作用、効果を有する。
However, in the method for producing a single layer synthetic resin film having the properties of a thermoplastic polyester film of the present invention, the amount of polyethylene resin in the film forming raw material influences the surface adhesive properties of the resulting film. A synthetic resin film with the desired surface adhesion depending on the application,
It has the function and effect that it can be easily obtained by changing the ratio between the thermoplastic polyester resin and the polyethylene resin in the film forming raw material.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明の合成樹脂製単層フィルムの製造方法に利用
される一般的なインフレーション法によるフィルム成形
機の縦断面略示図である。 1・・・’ff出機、2・・・ダイ、3,4・・ビンチ
ロール、5・・・成形工程中のチューブ状フィルム、6
・・巻取りロール。 特許出願人 大日本印刷株式会社 代理人 市 川 理 吉 同 新 井 清 子
The figure is a schematic longitudinal cross-sectional view of a film forming machine using a general inflation method used in the method for producing a single-layer synthetic resin film of the present invention. 1...'ff exit machine, 2... die, 3, 4... vinyl roll, 5... tubular film during the forming process, 6
...Take-up roll. Patent applicant Dai Nippon Printing Co., Ltd. Agent Osamu Kawa Doshin Kiyoko I

Claims (3)

【特許請求の範囲】[Claims] (1)熱可塑性ポリエステル樹脂20〜95重量%と、
ポリエチレン鎖を具備し、しかもエチレン含有率が50
重量%以上のポリエチレン系樹脂80〜5重量%との混
合樹脂を合成樹脂成分とする製膜用原料を、インフレー
ション法によるフィルム成形に付すことを特徴とする熱
可塑性ポリエステル製フィルムの性質を有する合成樹脂
製単層フィルムの製造方法。
(1) 20 to 95% by weight of thermoplastic polyester resin;
It has polyethylene chains and has an ethylene content of 50
Synthesis having the properties of a thermoplastic polyester film, which is characterized by subjecting a film-forming raw material whose synthetic resin component is a mixed resin with 80 to 5% by weight or more of a polyethylene resin to film formation by an inflation method. A method for producing a resin single-layer film.
(2)熱可塑性ポリエステル樹脂が、フタル酸。 イソフタル酸、テレフタル酸、マレイ/酸、マレイン酸
誘導体、コハク酸、アジピン酸、セバシン酸等の飽和多
塩基酸と、エチレングリコール、ジエテンングリコール
、グリセリン、トリメチロールプロパン、1,2−グロ
ビレングリコール、■、3−ブタンジオール、ジプロピ
レングリコール、1,4−ブタンジオール、1,6−ヘ
キサンジオール、ペンタエリスリット、ソルビトール、
ネオペンチルクリコール、L4−シクロヘキサンジメタ
ツール等の多価アルコールとのエステル結合によシ得ら
れるポリエステル樹脂である特許請求の範囲第1項記載
の熱可塑性ポリエステル製フィルムの性質を有する合成
樹脂製単層フィルムの製造方法。
(2) The thermoplastic polyester resin is phthalic acid. Saturated polybasic acids such as isophthalic acid, terephthalic acid, maleic acid, maleic acid derivatives, succinic acid, adipic acid, sebacic acid, and ethylene glycol, diethene glycol, glycerin, trimethylolpropane, 1,2-globylene glycol , ■, 3-butanediol, dipropylene glycol, 1,4-butanediol, 1,6-hexanediol, pentaerythritol, sorbitol,
A synthetic resin having the properties of a thermoplastic polyester film according to claim 1, which is a polyester resin obtained by ester bonding with a polyhydric alcohol such as neopentyl glycol or L4-cyclohexane dimetatool. Method for manufacturing single layer film.
(3) ポリエチレン鎖を具備し、しかもエチレン含有
率が50重量%以上のポリエチレン系樹脂が、高密度ポ
リエチレン、中密度ポリエチレン。 低密度ポリエチレン、エチレン−α−オレフィン共重合
体、エチレン−酢酸ビニル共重合体。 アイオノマー、エチレン−エチルアクリレート共重合体
、エチレ゛ンー酢酸ビニル共重合体ケン化物等のエチレ
ン重合体またはエチレン共重合体あるいはこれらの混合
物である特許請求の範囲第1項または第2項記載の熱可
塑性ポリエステル製フィルムの性質を有する合成樹脂製
単層フィルムの製造方法。
(3) The polyethylene resin having polyethylene chains and having an ethylene content of 50% by weight or more is high-density polyethylene or medium-density polyethylene. Low density polyethylene, ethylene-α-olefin copolymer, ethylene-vinyl acetate copolymer. The thermal compound according to claim 1 or 2, which is an ethylene polymer or ethylene copolymer, such as an ionomer, an ethylene-ethyl acrylate copolymer, a saponified ethylene-vinyl acetate copolymer, or a mixture thereof. A method for producing a single layer synthetic resin film having the properties of a plastic polyester film.
JP58159219A 1983-08-30 1983-08-30 Manufacture of synthetic resin mono-layered film having property of thermoplastic polyester film Pending JPS6049910A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58159219A JPS6049910A (en) 1983-08-30 1983-08-30 Manufacture of synthetic resin mono-layered film having property of thermoplastic polyester film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58159219A JPS6049910A (en) 1983-08-30 1983-08-30 Manufacture of synthetic resin mono-layered film having property of thermoplastic polyester film

Publications (1)

Publication Number Publication Date
JPS6049910A true JPS6049910A (en) 1985-03-19

Family

ID=15688932

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58159219A Pending JPS6049910A (en) 1983-08-30 1983-08-30 Manufacture of synthetic resin mono-layered film having property of thermoplastic polyester film

Country Status (1)

Country Link
JP (1) JPS6049910A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100704091B1 (en) * 2003-09-17 2007-04-05 닛토덴코 가부시키가이샤 Method of inflation extrusion molding, extrusion molding apparatus therefor, and process for producing pressure-sensitive adhesive sheet

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100704091B1 (en) * 2003-09-17 2007-04-05 닛토덴코 가부시키가이샤 Method of inflation extrusion molding, extrusion molding apparatus therefor, and process for producing pressure-sensitive adhesive sheet

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