JPS60178031A - Preparation of very thin polyethylene terephthalate film - Google Patents

Preparation of very thin polyethylene terephthalate film

Info

Publication number
JPS60178031A
JPS60178031A JP59032579A JP3257984A JPS60178031A JP S60178031 A JPS60178031 A JP S60178031A JP 59032579 A JP59032579 A JP 59032579A JP 3257984 A JP3257984 A JP 3257984A JP S60178031 A JPS60178031 A JP S60178031A
Authority
JP
Japan
Prior art keywords
film
polyethylene terephthalate
propylene copolymer
melting point
pet
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
JP59032579A
Other languages
Japanese (ja)
Other versions
JPH04453B2 (en
Inventor
Masayoshi Asakura
正芳 朝倉
Kazuhiro Tanaka
一博 田中
Yuji Okamura
岡村 右治
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP59032579A priority Critical patent/JPS60178031A/en
Publication of JPS60178031A publication Critical patent/JPS60178031A/en
Publication of JPH04453B2 publication Critical patent/JPH04453B2/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
    • B29D7/01Films 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
    • B29C55/02Shaping 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
    • 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
    • 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
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2009/00Layered products

Abstract

PURPOSE:To prevent orienting film from breaking by a method wherein a laminated oriented sheet of polyethylene terephthalate and propylene copolymer having a specified properties are heat-treated at a specified temperature and then cooled to peel them from each other. CONSTITUTION:Polyethylene terephthalate with intrinsic viscosities 0.55-0.75dl/g and propylene copolymer with intrinsic viscosities 1.0-2.0dl/g and melting points 100-150 deg.C are coextruded and then cooled to provide an unoriented laminated sheet. This unoriented laminated sheet is stretched in the uniaxial or biaxial direction, heat-treated at the temperature higher than the melting point of propylene copolymer and lower than that of polyethylene terephthalate, then, cooled down to the room temperature. Then, the polyethylene terephthalate film is peeled from the propylene copolymer layer to obtain a very thin polyethylene terephthalate film.

Description

【発明の詳細な説明】 (発明の技術分野) 本発明は極薄ポリエテレンテレフタシー1〜フイμ腸以
下のポリエチレンテレフタレートフィルムの製造方法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Technical Field of the Invention) The present invention relates to a method for producing an ultrathin polyethylene terephthalate film having a thickness of 1 to 5 mm.

〔従来技術およびその欠点〕[Prior art and its drawbacks]

極薄ポリエチレンテレフタレートフィルムの製造方法と
して、ポリエチレンテレフタレートとポリプロピレンを
共押出して積層し、これを延伸した後、ポリエチレンテ
レフタレートフィルムを剥離して作る方法は、特開昭5
7−176125.58−5226.58−13641
7号公報などに記載されており、公知である。
As a method for producing ultra-thin polyethylene terephthalate film, a method of co-extruding polyethylene terephthalate and polypropylene, laminating them, stretching this, and then peeling off the polyethylene terephthalate film was disclosed in Japanese Patent Laid-Open No. 5
7-176125.58-5226.58-13641
It is described in Publication No. 7, etc., and is well known.

しかし、かかる従来の方法では、延伸時のフィルム破れ
が多いこと、フィルム厚みむらが大きいこと、およびポ
リプロピレン層からポリエチレンテレフタレートフィル
ムを剥離する時の剥離性が劣ることという、3つの欠点
があった。
However, such conventional methods have three drawbacks: frequent film tearing during stretching, large film thickness unevenness, and poor peelability when peeling the polyethylene terephthalate film from the polypropylene layer.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、延伸中のフィルム破れが少なく、フィ
ルムの厚みむらが小さく、しかも剥離性に優れた極薄ポ
リエチレンテレフタレートフィルムの!I!J8方法を
Imm(rA、、L−tAlF)−FAA−〔発明の構
成〕 本発明は、上記目的を達成するため、次の構成、すなわ
ち、極限粘度0,55〜0.75dα/9のポリエチレ
ンテレフタレートと、極限粘瓜1゜0〜2.0dQ/Q
、融点100〜150℃のプロピレン共重合体とを共押
出して積層シートとし、これを−軸または二軸方向に延
伸し、次いで、プロピレン共重合体の融点より高く、か
つポリエチレンテレフタレートの融点より低い温度で熱
処理した後、室温まで冷却し、次にポリエチレンテレフ
タレートフィルムをプロピレン共重合体層から剥111
 iる極薄ポリエチレンテレフタレートフィルムの製造
り法を骨子するものである。
The object of the present invention is to create an ultra-thin polyethylene terephthalate film that has less tearing during stretching, less uneven film thickness, and excellent peelability! I! J8 method Imm(rA,,L-tAlF)-FAA- [Structure of the invention] In order to achieve the above object, the present invention has the following structure, namely, polyethylene having an intrinsic viscosity of 0.55 to 0.75 dα/9. Terephthalate and extreme viscosity 1゜0~2.0dQ/Q
, a propylene copolymer with a melting point of 100 to 150°C is coextruded to form a laminated sheet, which is stretched in the -axial or biaxial direction, and then is higher than the melting point of the propylene copolymer and lower than the melting point of polyethylene terephthalate. After heat treatment at temperature, the polyethylene terephthalate film is cooled to room temperature and then peeled off from the propylene copolymer layer.
This article outlines a method for producing an ultra-thin polyethylene terephthalate film.

本発明におりるポリエチレンテレフタレートとは、分子
量M成の90モル%以上がエチレンテレフタレート11
1位からなるポリマであり、その極限粘ffj G;&
 0 、55〜0 、75 d D、 / Q、好まし
くは、0.58〜0.70(J(1/Q(Dflu囲の
もノテある。
Polyethylene terephthalate according to the present invention means that 90 mol% or more of the molecular weight M is ethylene terephthalate 11.
1, and its limiting viscosity ffj G; &
0,55~0,75 dD,/Q, preferably 0.58~0.70(J(1/Q(Dflu).

極限粘度が上記範囲より大きくても小さくても、フィル
ムの厚みむらが大きくなるので本発明目的に合致しなく
なる。もちろん、エチレンテレフタレート単位が90モ
ル%以下にならない範囲で、公知の共重合分子単位、例
えば、エチレンイソフタレート、ブチレンテレフタレー
ト、エチレンアジベート、エチレンレバケート、ポリエ
チレングリコールなどを共重合したものも、本発明でい
うポリエチレンテレフタレートの中に含まれる。
If the intrinsic viscosity is larger or smaller than the above range, the film will have a large thickness unevenness, which will not meet the purpose of the present invention. Of course, copolymerization of known copolymerized molecular units, such as ethylene isophthalate, butylene terephthalate, ethylene adipate, ethylene rebacate, polyethylene glycol, etc., may also be used as long as the ethylene terephthalate unit does not become less than 90 mol%. It is included in the polyethylene terephthalate referred to in the invention.

また、このポリエチレンテレフタレートには、公知の添
加剤、例えば有機または無機微粒子、顔料、可塑剤、ワ
ックス類、酸化防止剤、紫外性吸収剤、帯電防止剤など
を目的に応じて添加してもよい。(なお、以竣の説明で
は、ポリエチレンテレフタレートをPETと略称する。
Further, known additives such as organic or inorganic fine particles, pigments, plasticizers, waxes, antioxidants, ultraviolet absorbers, antistatic agents, etc. may be added to this polyethylene terephthalate depending on the purpose. . (In the following explanation, polyethylene terephthalate will be abbreviated as PET.

) プロピレン共重合体とは、プロピレン80〜97モル%
と、プロピレン以外のオレフィン3〜20モル%との共
重合体からなるポリマであり、具体例としては、プロピ
レン・エチレン共重合体、プロピレン・ブテン共重合体
、プロピレン・ヘキセン共重合体、プロピレン・エチレ
ン・ブテン三元共重合体あるいはこれらの混合物などを
あげることができる。共重合様式としては、ランダム共
重合体であることが望ましいが、ブロック共重合体も、
プlコックの程度によっては使用覆ることができる。な
お、プロピレン共重合体と他のポリオレフィン(例えば
ボリエチレン、ポリブテンなど)との混合物であっても
、プロピレン共重合体が該混合物の50重量%以上、好
ましくは75重量%以上を占めていれば、本発明でいう
プロピレン共重合体の範囲に含めることができる。
) Propylene copolymer is propylene 80-97 mol%
and 3 to 20 mol% of olefin other than propylene. Specific examples include propylene/ethylene copolymer, propylene/butene copolymer, propylene/hexene copolymer, propylene/ Examples include ethylene-butene terpolymers and mixtures thereof. As for the copolymerization mode, a random copolymer is preferable, but a block copolymer can also be used.
It can be used depending on the degree of pluck. In addition, even if it is a mixture of propylene copolymer and other polyolefins (e.g. polyethylene, polybutene, etc.), if the propylene copolymer accounts for 50% by weight or more, preferably 75% by weight or more of the mixture, It can be included in the scope of the propylene copolymer referred to in the present invention.

本発明で用いるプロピレン共重合体の極限粘度は1.O
〜2.0dfl/gll?ましくは1.2〜1.8dα
/gの範囲にあることが必政である。
The intrinsic viscosity of the propylene copolymer used in the present invention is 1. O
~2.0dfl/gll? Preferably 1.2 to 1.8 dα
/g is essential.

この範囲より外れると、フィルムの厚みむらが悪(なる
ので、本発明目的に合致しなくなる。
If it is outside this range, the film will have poor thickness unevenness, which will not meet the purpose of the present invention.

また、プロピレン共重合体の融点は、100〜150℃
、好ましくは105〜140℃、さらに好ましくは11
0〜135℃の範囲にあることが心数である。この範囲
を外れると、延伸中のフィルム破れの頻瓜が増加するの
で好ましくない。
In addition, the melting point of propylene copolymer is 100 to 150°C
, preferably 105 to 140°C, more preferably 11
The number of cores is within the range of 0 to 135°C. If it is outside this range, the frequency of film breakage during stretching increases, which is not preferable.

RPCと略称する。) 本発明では、PETとRPCを別々の押出機に供給して
、200〜300℃の押出温度で溶融押出し、溶融体同
志をポリマ管内部あるいは口金内部で合流させて積層状
態とし、口金から積層シートとして押出す(これを共押
出という)。この積層シートは、PET/RPCの2層
でもよく、PET/PPC/PETの3層でもよく、あ
るいは1) E T / P P C/ P E T 
/ P P C/ P E Tのように5層でもよい。
It is abbreviated as RPC. ) In the present invention, PET and RPC are supplied to separate extruders, melt-extruded at an extrusion temperature of 200 to 300°C, the melts are merged inside the polymer tube or the nozzle to form a layered state, and the lamination is carried out from the nozzle. Extrude as a sheet (this is called coextrusion). This laminated sheet may be two layers of PET/RPC, three layers of PET/PPC/PET, or 1) E T / P P C / P E T
/PPC/PET may have five layers.

いずれにしても、PET層が最外層の少なくとも片側に
存在することが望ましい。
In any case, it is desirable that a PET layer be present on at least one side of the outermost layer.

そうでないと、延伸後の熱処理において、フィルムが歪
みやずく、厚みむらが悪化する傾向がある。
Otherwise, in the heat treatment after stretching, the film tends to become distorted, cracked, and have uneven thickness.

共押出された溶融積層シートを表面温度10〜60℃の
冷却ドラムに巻きつけて、20〜70℃まで冷却して固
化し、未延伸積層シートとする。この冷却同化に際して
、溶融シートの上面に、1〜15KVの直流高電圧を印
加したワイアを配置して、この電荷により、溶融シート
をドラムに押し層シートが得られる。このシートを80
〜130℃、Ilfましくは90〜120℃に加熱して
一軸方向に3〜5倍延伸J′る。この延伸は2〜3段階
に分りで行ってもよい。次に、二軸延伸の場合には、上
記の一軸延伸フイルムを前と直角方向に、延伸速度1,
000〜10,000%/分にて、3゜5〜6倍延伸す
る。この場合の延伸温度は、前の一軸延伸時の温度より
5〜20°C高目にすることが望ましい。また、別の手
法として、上記未延伸積層シー1−を80〜130℃、
好ましくは90〜120℃に加熱して、二軸方向同時に
各々3〜5償延伸して、二軸延伸してもにい。また、二
軸延伸されたフィルムを再度、いずれかのIj向へ1゜
1〜2.0倍、再延伸してもよい。
The coextruded molten laminated sheet is wound around a cooling drum with a surface temperature of 10 to 60°C, and cooled to 20 to 70°C to solidify it to form an unstretched laminated sheet. During this cooling and assimilation, a wire to which a direct current high voltage of 1 to 15 KV is applied is placed on the upper surface of the molten sheet, and the molten sheet is pressed against a drum by this electric charge to obtain a layered sheet. This sheet is 80
The film is heated to 130 DEG C., preferably 90 DEG to 120 DEG C., and stretched 3 to 5 times in the uniaxial direction. This stretching may be performed in two to three stages. Next, in the case of biaxial stretching, the above-mentioned uniaxially stretched film is stretched in a direction perpendicular to the front direction at a stretching speed of 1,
Stretched at 3° and 5 to 6 times at a rate of 000 to 10,000%/min. The stretching temperature in this case is preferably 5 to 20°C higher than the temperature during the previous uniaxial stretching. In addition, as another method, the above unstretched laminated sheet 1- is heated at 80 to 130°C.
Preferably, the film may be biaxially stretched by heating to 90 to 120°C and simultaneously stretching in both directions for 3 to 5 degrees. Further, the biaxially stretched film may be re-stretched by 1°1 to 2.0 times in either Ij direction.

次に、この延伸された積層フィルムを、l) l) C
のUit点以上、PETの融点以下の温度に加熱して、
1−20秒間、好ましくは2〜10秒間熱処理り−る。
Next, this stretched laminated film is
Heating to a temperature above the Uit point of PET and below the melting point of PET,
Heat treatment is performed for 1-20 seconds, preferably 2-10 seconds.

この熱処理は、フィルムを緊張状態に保持しlこまま行
って−bJ:いか、延伸終了後の面積を塁準にして、2
〜15%の面積弛緩率を与えつつ熱処理した方が、後で
PETフィルムを剥離する時の剥離性が良好になるので
好ましい(面積弛緩率の計算例:延伸終了後のフィルム
面(a100o#のちのが、熱処理中に、−軸方向また
は二軸方向に微かの弛緩を受けて収縮し、熱処理終了後
の面積が96fflになっていたとすれば、面積弛緩率
は4%である)。なお、この熱処理温度がRPCの融点
より低いと、後でPETフィルムを剥離する時の剥離性
が悪くなるので好ましくなく、また逆に、1) E T
の融点より高いど、PETフィルムが白濁して脆くなり
、やはり剥離ができなくなるので好ましくない。
This heat treatment is performed by keeping the film under tension and using the area after stretching as a standard.
It is preferable to perform heat treatment while giving an area relaxation rate of ~15%, as this will improve the peelability when peeling the PET film later (Example of calculation of area relaxation rate: film surface after stretching (a100o#) However, during the heat treatment, if it undergoes slight relaxation in the -axis direction or biaxial direction and contracts, and the area after the heat treatment is 96 ffl, the area relaxation rate is 4%). If this heat treatment temperature is lower than the melting point of RPC, it is not preferable because the releasability when peeling off the PET film later becomes poor, and conversely, 1) E T
If the temperature is higher than the melting point of , the PET film will become cloudy and brittle, making it impossible to peel it off, which is not preferable.

次に、熱処理された積層フィルムを室温、つまり、通常
20〜40℃まで徐冷する。冷7JIは、空気や水で行
ってもよく、あるいは、冷却ロールに接触させて冷却し
てもよい。なJ3、冷却されたフィルムを、その温度の
まま、あるいは再度、加熱ロールで50〜90℃に加熱
して、フィルムの片面または両面にコロナ放電処理を行
なってもよい。
Next, the heat-treated laminated film is slowly cooled to room temperature, typically 20 to 40°C. Cold 7JI may be performed with air or water, or may be cooled by contacting with a cooling roll. J3, the cooled film may be kept at that temperature or heated again to 50 to 90°C with a heating roll to perform corona discharge treatment on one or both sides of the film.

この処理によって、後からのPETフィルムの剥離が容
易になる場合がある。かくして得られた積層フィルムか
ら、PETフィルムを剥離して、通常厚さ0.2〜4μ
nl 、好ましくはJワさ0.2〜2μmのA R9P
 E 1−フィルムを得る。この剥離方法は特に限定さ
れるものではないが、vi層フィルムを1組のニップロ
ール間にニップし、この片側のロール表面にPETフィ
ルムが沿っていく形で剥離すると、連続剥liI+が容
易である。また、積層フィルムl) E T面に、印刷
、ラミネー1〜、]〜テルティンるいは蒸着を施した後
、PETフィルムを剥離してらj:い。いずれの場合で
も、剥離する1’) r二TフィルLx表面の静電気を
、静電除去器などを用いて除去しておくことが剥離を容
易にづるうえでΦ要Cある。
This treatment may make it easier to peel off the PET film later. The PET film is peeled off from the laminated film thus obtained, and the thickness is usually 0.2 to 4 μm.
nl, preferably A R9P with a J diameter of 0.2 to 2 μm
E 1 - Obtain a film. This peeling method is not particularly limited, but continuous peeling is easy if the VI layer film is nipped between a set of nip rolls and the PET film is peeled along the surface of one of the rolls. . In addition, after printing, lamination 1, ], tertin or vapor deposition is applied to the ET side of the laminated film, the PET film is peeled off. In either case, it is essential to remove static electricity on the surface of the T-fill Lx to be peeled off using a static eliminator or the like in order to facilitate peeling.

/、@ A3、本発明は上記のごとき方法を特徴とする
しのであるが、P )) C層中に、C)、001〜1
徂fij 96、llr マL < I、L O、OO
5〜0 、5 ’A L3− % (7)非ネ)“Ir
系滑剤を含イ]I!シめてJ3<ことににす、1つE′
[フィルムの剥離性をさらに良好にすることができる。
/, @A3, The present invention is characterized by the above method, but in the P)) C layer, C), 001-1
徂fij 96, llr ma L < I, L O, OO
5~0, 5'A L3-% (7) Non-Ne) "Ir
Contains lubricant] I! Shitte J3<especially one E'
[The releasability of the film can be further improved.

)1三ネ\°l子系滑剤とは、PPCの溶融押出温石に
J3いて、液体あるいは溶融体である物質で、それの添
加によってppcライルムの滑性を向上せしめうるちの
を意味し、具体例を示せば、次のような物質である。な
お、これらの物質の2種類以上がフィルム中に含有され
ている場合は、それらの合計(6)が上記含有量範囲に
あればよい。
) 1 Sanne\°l lubricant is a liquid or molten substance that is added to PPC melt-extruded hot stones, and its addition improves the lubricity of PPC limestone. Examples include the following substances: In addition, when two or more types of these substances are contained in the film, their total (6) should just be within the above content range.

A、脂肪族炭化水素 流動パラフィン、マイクロクリスタリンワックス、天然
パラフィン、合成パラフィン、ポリエチレンワックス、
ポリプロピレンワックスなど。
A, aliphatic hydrocarbon liquid paraffin, microcrystalline wax, natural paraffin, synthetic paraffin, polyethylene wax,
polypropylene wax etc.

B、高級脂肪酸またはその金属塩 ステアリン酸、ステアリンffQ /Jルシウム、じド
ロキシステアリン酸、硬化油、モンタン酸ナトリウムな
ど。
B, higher fatty acid or its metal salt stearic acid, stearin ffQ/J lucium, didroxystearic acid, hydrogenated oil, sodium montanate, etc.

C1脂肪酸アミド ステアリン酸アミド、オレイン酸アミド、エルカ酸アミ
ド、リシノール酸アミド、ベヘンアミド、メチレンピス
ステアラミドなど。
C1 fatty acid amide stearamide, oleic acid amide, erucic acid amide, ricinoleic acid amide, behenamide, methylene pistearamide, etc.

D、脂肪酸エステル 「1−ブチルステアレート、メチルヒドロキシステアレ
ート、ミリシルセロチネート、多価アルコール脂肪酸エ
ステル、エステル系ワックスな乙 1三、脂肪酸りトン ケ1〜ンワックスなど。
D. Fatty acid esters: 1-butyl stearate, methyl hydroxystearate, myricyl cerotinate, polyhydric alcohol fatty acid esters, ester waxes, fatty acid ester waxes, etc.

[、脂肪アルコール ラウリルアルコール、スデアリルアルコール、ミリスヂ
ルアルコール、セヂルアルコールなど。
[, fatty alcohols lauryl alcohol, sudearyl alcohol, myrisudyl alcohol, cedyl alcohol, etc.

G、脂肪酸と多IJliアルコールの部分エステルグリ
セリン脂肪酸エステル、ヒドロキシステアリンM l〜
リグリレリド、ソルビタン脂肪酸ゴスチルなど。
G, Partial ester of fatty acid and poly-IJli alcohol Glycerin fatty acid ester, Hydroxystearin M l~
Liguleride, sorbitan fatty acid gostil, etc.

1」、非イオン系界面活性剤 ポリオキシエチレンアルギルエーテル、ポリオ−1ニシ
エブーレンフエニルエーテル、ポリオキシ]二チレンj
I)し4ニルアミド、ボリオギシエチレン1指肋酸Jス
テルなど。
1", nonionic surfactant polyoxyethylene argyl ether, polyol-1-nitheburene phenyl ether, polyoxy] dithylene j
I) 4-silamide, boriogythyethylene 1-digital acid J ster, etc.

1、シリコン油 直鎖状メチルシリコン油、メチシフlニルシリコン油、
変性シリコン油など。
1. Silicone oil linear methyl silicone oil, methifurnyl silicone oil,
Modified silicone oil etc.

J、フッ素系界面活性剤 フルオロアルキルカルボン ルキルカルボン酸、モノパーフルオロアルキルエヂルリ
ン酸エステル、パーフルオロアルキルスルホン酸塩など
J, fluorosurfactants such as fluoroalkylcarbonylcarboxylic acid, monoperfluoroalkyl edyl phosphate, perfluoroalkyl sulfonate, etc.

なお、上記の非粒子系滑剤と併用して、平均粒径0.0
01〜2μmの無機微粒子、例えば、乾式シリカ、湿式
シリカ、ゼオライト、炭酸カルシウム、リン酸カルシウ
ム、カオリン、カオリナイト、クレイ、タルク、酸化チ
タン、アルミナ、ジルコニア、水酸化アルミニウムなど
の粒子系滑剤を、l) P Cフィルム中に0.01〜
0.5重量%含有せしめておくと、非粒子系滑剤の効果
を相乗的に高めうる場合が多い。
In addition, when used in combination with the above non-particulate lubricant, an average particle size of 0.0
01-2 μm inorganic fine particles, such as dry silica, wet silica, zeolite, calcium carbonate, calcium phosphate, kaolin, kaolinite, clay, talc, titanium oxide, alumina, zirconia, aluminum hydroxide, etc., as particulate lubricants, l) 0.01~ in PC film
When the content is 0.5% by weight, the effect of the non-particulate lubricant can often be enhanced synergistically.

〔発明の効果〕〔Effect of the invention〕

本発明は、上述したとおり特定の物性を持っPETとR
PCを共押出し、延伸後、特定温度範囲で熱処理し、次
いで、PETフィルムを剥離して、極ii9 P E 
1−フィルムを製造する方法としたので、延伸中のフィ
ルム破れ頻度の減少、フィルムの厚みむらの減少J3よ
びPFTフィルムを剥離する時の剥lift性の向上と
いう効果が得られ、極薄PETフィルムを安定して製造
できるようになった。かくして得られた極薄P E 1
−フィルムは、コンデンリー用11六電休、孔版印刷用
II;1紙あるいはタイプライタ−リボン用ベースフィ
ルムなど多くの用途に用いることができる。
The present invention utilizes PET and R with specific physical properties as described above.
After coextruding PC and stretching, it is heat-treated in a specific temperature range, and then the PET film is peeled off to form a polar ii9 P E
1-The method for producing the film has the following effects: a reduction in the frequency of film breakage during stretching, a reduction in film thickness unevenness, and an improvement in peelability when peeling the PFT film. It has become possible to stably manufacture . The ultrathin P E 1 thus obtained
- The film can be used for many purposes, such as base film for condenser printing, II for stencil printing, paper or typewriter ribbon.

〔物性の測定方法J3よび評価基準〕 本発明にJ3いて用いた物性などの測定方法および各特
性の評価基準は次のとおりである。
[Measurement method J3 of physical properties and evaluation criteria] The measurement method J3 of physical properties and the evaluation criteria of each property used in the present invention are as follows.

(1)PlETの(Φ限粘度 25℃のAルソクロ1」フェノールにI) E 1−を
溶解して、、信法ににり極I尺粘度を測定した。
(1) PlET (I) E 1- was dissolved in phenol with a limiting viscosity of 25° C., and the ultimate viscosity was measured using the Shin method.

(2) P P Cの極限粘度 ASTM−Dl (301の極限粘度を用いた。(2) Intrinsic viscosity of P P C ASTM-Dl (intrinsic viscosity of 301 was used.

(3)融点 1) S Cを用いで、20℃/分のシー湯速1哀ぐ昇
温していき、Itii!解にとしなう吸熱ピークの頂上
部に相当りる温度を融点どした(試料ffl : 1 
01B)。
(3) Melting point 1) Using SC, heat the water at a rate of 20°C/min. The melting point was defined as the temperature corresponding to the top of the endothermic peak that corresponds to the solution (sample ffl: 1
01B).

なお、融1+.tのピークが2つ以上でる時は、高さの
高い方のピークの頂上部の温度を融点とした。
In addition, fusion 1+. When two or more peaks of t appeared, the temperature at the top of the higher peak was taken as the melting point.

(4) フィルム破れ頻度 二軸延伸製膜を8時間連続して行なった時のフィルム破
れの起こった回数で表示した。従って、単位は、回/8
’11.’1間Cある。通’7;’、この(的が2回/
8時間以下でないと、実用化はむずかしい。
(4) Frequency of film breakage The frequency of film breakage was expressed as the number of times film breakage occurred during continuous biaxial stretching film formation for 8 hours. Therefore, the unit is times/8
'11. 'There is one C. '7;', this (target twice/
Unless it is 8 hours or less, it is difficult to put it into practical use.

(5) フィルムの厚みむら 熱処理され、冷却された積層フィルムの、フィルム幅方
向の厚さを、電子式フィルム厚さi+で連続測定する(
フィルム幅1m)。この中で最も厚い部分の厚さと、最
も薄い部分の厚さとの差を、平均厚さで割り、これに1
00を乗じて、厚みむら(%)とする。通常、この値が
10%以下でないと、実用性に乏しいと占える。
(5) Film thickness unevenness The thickness of the heat-treated and cooled laminated film in the film width direction is continuously measured using an electronic film thickness i+ (
Film width 1m). Divide the difference between the thickness of the thickest part and the thickness of the thinnest part by the average thickness, and add 1
Multiply by 00 to obtain thickness unevenness (%). Usually, if this value is less than 10%, it is considered to be impractical.

’([3)PETフィルムの剥離性 得られた積層フィルムから、10m/分の剥離速瓜でl
) E−1−フィルムを連続剥離し、次の3つの評価i
!準で評価した。
'([3) Peelability of PET film From the obtained laminated film, l
) E-1-Continuously peel the film and evaluate the following three
! Evaluated based on standard.

゛良好″:フィルム切れや破れの発生がなく、500m
以上連続剥離できたもの。
``Good'': No film cut or tear, 500m
Those that were able to be peeled off continuously.

゛′酋通”:100〜300m位は連続剥離できるが、
それ位で、フィルム切れ−1b破れを生じるもの。
゛′酋通”: Continuous peeling is possible for about 100 to 300 meters, but
At that level, the film will break - 1b will tear.

゛′不良”:10〜90m位しか連続剥離できないもの
``Poor'': Continuous peeling of only about 10 to 90 m is possible.

なお、当然ながら、剥離性は゛良好゛′でないと、実用
1りに乏しいと言える。
Of course, it can be said that if the releasability is not "good", it will be of poor practical use.

〔実施例a3よび比較例〕 以下、実施例J’; J:び比較例によって、本発明の
一実副態様を説明する。
[Example a3 and Comparative Examples] Hereinafter, one embodiment of the present invention will be explained using Examples J'; J: and Comparative Examples.

実施例1 下記2(jト類の原オ′31(ペレツ1〜)を県(+i
ii した。
Example 1 The following 2
ii I did.

P E T :ポリ」ニチレンテレフタレ−1−のホモ
ポリマ。極限粘度0.62dfl/g、fMi点259
 ”C,。
PET: Homopolymer of poly'nitylene terephthalate-1-. Intrinsic viscosity 0.62 dfl/g, fMi point 259
"C.

P P C: ’Lチレン含右吊6更量%のプロピレン
・エチレン・ランダム共m台体。極限粘度1 、656
71/ <7 。H11点120″coコール力酸jノ
ミド0.3徂Φ%および平均粒径0.9μmの炭酸カル
シウム0.3車量%を含有している。
P P C: 'L-ethylene-containing propylene-ethylene random co-base with 6% by weight. Intrinsic viscosity 1, 656
71/<7. It contains 0.3 x Φ% of H11 point 120'' cocolic acid nomide and 0.3% of calcium carbonate with an average particle size of 0.9 μm.

この2種類の原料を各々別の押出機に供給して、PET
を280’CXPPCを260℃で溶融押出し、各々の
溶融体をT型口金の中で合流せしめて、P E −r 
/ P P Cの2層(に成とし、これを30℃の冷却
ドラムに巻きつけて、8KVの直流高電圧を印加しつつ
冷却固化ぜしめ、2層積層シー1〜とした。このシート
を90°Cに加熱した後、長手方向に3.1B延伸し、
ただちに30℃まで冷7Jl シた。
These two types of raw materials are each fed to separate extruders to produce PET
280'C
/ P P C (2 layers) was wound around a cooling drum at 30°C, and cooled and solidified while applying a DC high voltage of 8 KV to form two-layer laminated sheets 1 to 1. This sheet was After heating to 90°C, stretching 3.1B in the longitudinal direction,
Immediately cooled down to 30℃ for 7Jl.

次いで、再度100℃に加熱して、幅方向に延伸速度2
,500%/分にて5.0倍延伸し、そのまま温度を2
15°Cまで上げて、5秒間熱処理した。この熱処理区
間内にJ3いて、面積弛緩率5%の弛緩処理を行なった
。このフィルムを室温まで徐冷して、静電除去器で静電
気を除去しつつ巻取った。かくし得られた積層フィルム
は、PET層1.0μ、PP0層10μmの構成となっ
ていた。
Next, it was heated to 100°C again and stretched at a speed of 2 in the width direction.
, stretched 5.0 times at 500%/min, then lowered the temperature to 2
The temperature was raised to 15°C and heat treated for 5 seconds. J3 was located within this heat treatment section, and relaxation treatment was performed with an area relaxation rate of 5%. This film was slowly cooled to room temperature and wound up while removing static electricity using a static eliminator. The thus obtained laminated film had a PET layer of 1.0 μm and a PP0 layer of 10 μm.

このフィルムを連続製膜した時のフィルム破れ頻度はO
回/8時局、フィルムの厚みむらは5%と、いずれも良
好であった。次に、この積層フィルムから、P]三丁フ
ィル11を列間してみICところ、500+u以上連続
して剥離で゛き、剥離性(よ゛良好“′であったっ 比較例1 実施例1のl) P Cのかわりに、極限粘度2.3d
σ/gのl) l−’ Cを用いてみた(RPCの他の
特性は、実施例1と同じ)。他はすべて実施例1と同様
にして製膜したところ、フィルムの厚みむらが25%と
非常に劣ったしのと41つ7C。
The frequency of film tearing when this film was continuously formed was O
At 8 o'clock, the thickness unevenness of the film was 5%, which was good. Next, from this laminated film, P] Sancho Fill 11 was applied between the rows, and the IC was able to be peeled off continuously over 500+U, and the peelability (very good) was obtained. Comparative Example 1 Example 1 l) Instead of PC, the intrinsic viscosity is 2.3d.
σ/g l) l−' C was used (other characteristics of RPC are the same as in Example 1). When a film was formed in the same manner as in Example 1, the thickness unevenness of the film was very poor at 25%.

比較例2 比較例1どは逆に、極限粘度0.8dα/qのP l)
 Cを用い、他(よ比較例1(実施例1)と同様にして
製膜してみたところ、フィルムの厚みむらが32%とJ
l 7i’、に劣ったものになり、しかし、フィルl\
破れ頻度し6回/8時間と多くなった。
Comparative Example 2 On the contrary, Comparative Example 1 etc. had P l) with an intrinsic viscosity of 0.8 dα/q.
When a film was formed using C in the same manner as in Comparative Example 1 (Example 1), the film thickness unevenness was 32%.
l 7i', but it becomes inferior to Phil l\\
The frequency of breakage increased to 6 times/8 hours.

比較例3 実施1911のl’ I) Cの1−チレン含イj量を
変更して、融点155°Cおよび融点95℃のRPCを
用い、他は実施例1ど同様にして製膜したところ、いず
れのl) l) Cを用いても、フィルム破れMi +
夏が20回/8時間以上と極めて破れやづく、実用性に
乏しいものであった。
Comparative Example 3 A film was formed in the same manner as in Example 1 except that the 1-tyrene content of l' I) C of Example 1911 was changed and RPC with a melting point of 155°C and a melting point of 95°C was used. , any l) l) Even if C is used, film tearing Mi +
It was worn over 20 times in the summer for 8 hours or more, and was extremely prone to tearing, making it impractical.

比較例4 実施例1のP E Tのかわりに、極限粘度0.50お
よび0.80d0./gのPETを用い、他の条件は実
施例1と同様にして製膜してみたどころ、いずれのPE
Tを用いても、フィルムの厚みむらが20%以上と非常
に悪いものになっlこ。
Comparative Example 4 Instead of PET in Example 1, intrinsic viscosities of 0.50 and 0.80d0. /g of PET and the other conditions were the same as in Example 1.
Even if T was used, the thickness unevenness of the film was extremely poor, exceeding 20%.

比較例5 実施例1にd3いて、延伸後の熱処理温度を110°C
とし、他の条件はそのままにして製膜してみた。得られ
た積層フィルムの剥離性を評価したところ、パ普通″で
あり、やや実用性に欠けるものであった。
Comparative Example 5 d3 in Example 1, heat treatment temperature after stretching was 110°C
I tried forming a film with the other conditions unchanged. When the peelability of the obtained laminated film was evaluated, it was found to be "fair" and somewhat lacking in practicality.

特許出願人 東 し 株 式 会 社Patent applicant Higashi Shikikai Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 極限粘度0.55〜0.75dα/gのポリエチレンテ
レフタレートと、極限粘度1.0〜2゜Odα/g、融
点100〜150℃のプロピレン共重合体とを共押出し
て積層シートとし、これを一軸または二輪方向に延伸し
、次いで、プロピレン共重合体の融点J:り高く、かつ
ポリエチレンテレフタレートの融点より低い温度で熱処
理した後、室温まで冷却し、次にポリエチレンテレフタ
レートフィルムをプロピレン共重合体層から剥離する極
薄ポリエチレンテレフタレートフィルムの製造方法。
Polyethylene terephthalate with an intrinsic viscosity of 0.55 to 0.75 dα/g and a propylene copolymer with an intrinsic viscosity of 1.0 to 2° Odα/g and a melting point of 100 to 150°C are coextruded to form a laminated sheet, which is uniaxially Alternatively, the polyethylene terephthalate film is stretched in the two-wheel direction, then heat treated at a temperature higher than the melting point J of the propylene copolymer and lower than the melting point of polyethylene terephthalate, cooled to room temperature, and then the polyethylene terephthalate film is separated from the propylene copolymer layer. A method for producing an ultra-thin polyethylene terephthalate film that can be peeled off.
JP59032579A 1984-02-24 1984-02-24 Preparation of very thin polyethylene terephthalate film Granted JPS60178031A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59032579A JPS60178031A (en) 1984-02-24 1984-02-24 Preparation of very thin polyethylene terephthalate film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59032579A JPS60178031A (en) 1984-02-24 1984-02-24 Preparation of very thin polyethylene terephthalate film

Publications (2)

Publication Number Publication Date
JPS60178031A true JPS60178031A (en) 1985-09-12
JPH04453B2 JPH04453B2 (en) 1992-01-07

Family

ID=12362785

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59032579A Granted JPS60178031A (en) 1984-02-24 1984-02-24 Preparation of very thin polyethylene terephthalate film

Country Status (1)

Country Link
JP (1) JPS60178031A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0271066A2 (en) * 1986-12-12 1988-06-15 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Method of preventing expansioninduced wrinkles of plastic film and metal foil
JPS63205324A (en) * 1987-02-20 1988-08-24 Toray Ind Inc Production of plastic film
JPS649235A (en) * 1987-07-01 1989-01-12 Toppan Printing Co Ltd Production of film
US5089341A (en) * 1989-01-12 1992-02-18 Asahi Kasei Kogyo Kabushiki Kaisha High-sensitivity thermosensitive multilayer film and method for production of plate-making stencil sheet
JPH05293885A (en) * 1991-02-22 1993-11-09 Osaka Kasei Kk Sheet consisting of low viscosity polyester resin and its manufacture
EP0808713A3 (en) * 1996-05-24 1999-04-28 Teijin Limited Biaxially oriented multilayered film
GR980100321A (en) * 1998-08-25 2000-04-27 Plastic film production by peeling off the various layers of multi-layer films
EP1616689A1 (en) * 2003-03-28 2006-01-18 Mitsui Chemicals, Inc. Stretched film and method for production thereof
JP2011173391A (en) * 2010-02-25 2011-09-08 Polytech Inc Method of manufacturing easy delamination sheet and delamination sheet obtained by the method
JP2012136027A (en) * 2012-02-16 2012-07-19 Polytech Inc Easy delamination sheet

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5729033B2 (en) * 2011-03-15 2015-06-03 凸版印刷株式会社 Method for producing thin film

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0271066A2 (en) * 1986-12-12 1988-06-15 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Method of preventing expansioninduced wrinkles of plastic film and metal foil
JPS63205324A (en) * 1987-02-20 1988-08-24 Toray Ind Inc Production of plastic film
JPS649235A (en) * 1987-07-01 1989-01-12 Toppan Printing Co Ltd Production of film
US5089341A (en) * 1989-01-12 1992-02-18 Asahi Kasei Kogyo Kabushiki Kaisha High-sensitivity thermosensitive multilayer film and method for production of plate-making stencil sheet
JPH05293885A (en) * 1991-02-22 1993-11-09 Osaka Kasei Kk Sheet consisting of low viscosity polyester resin and its manufacture
EP0808713A3 (en) * 1996-05-24 1999-04-28 Teijin Limited Biaxially oriented multilayered film
US5932341A (en) * 1996-05-24 1999-08-03 Teijin Limited Biaxially oriented multilayered film
GR980100321A (en) * 1998-08-25 2000-04-27 Plastic film production by peeling off the various layers of multi-layer films
EP1616689A1 (en) * 2003-03-28 2006-01-18 Mitsui Chemicals, Inc. Stretched film and method for production thereof
EP1616689A4 (en) * 2003-03-28 2010-07-14 Mitsui Chemicals Inc Stretched film and method for production thereof
JP2011173391A (en) * 2010-02-25 2011-09-08 Polytech Inc Method of manufacturing easy delamination sheet and delamination sheet obtained by the method
JP2012136027A (en) * 2012-02-16 2012-07-19 Polytech Inc Easy delamination sheet

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