JPH04455B2 - - Google Patents

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Publication number
JPH04455B2
JPH04455B2 JP60081409A JP8140985A JPH04455B2 JP H04455 B2 JPH04455 B2 JP H04455B2 JP 60081409 A JP60081409 A JP 60081409A JP 8140985 A JP8140985 A JP 8140985A JP H04455 B2 JPH04455 B2 JP H04455B2
Authority
JP
Japan
Prior art keywords
stretching
film
longitudinal
stage
temperature
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.)
Expired - Lifetime
Application number
JP60081409A
Other languages
Japanese (ja)
Other versions
JPS61241128A (en
Inventor
Hideaki Watanabe
Atsushi Niki
Satoyuki Nakamura
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP8140985A priority Critical patent/JPS61241128A/en
Publication of JPS61241128A publication Critical patent/JPS61241128A/en
Publication of JPH04455B2 publication Critical patent/JPH04455B2/ja
Granted legal-status Critical Current

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  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

技術分野 本発明は二軸延伸ポリエチレンテレフタレート
フイルムの製造方法に関するものであり、更に詳
しくは縦(フイルムの長手方向)、横(フイルム
の幅方向)両方向ともに機械特性が高められた二
軸延伸ポリエチレンテレフタレートフイルムの製
造方法に関する。 従来技術とその問題点 ポリエチレンテレフタレート(以下PETと略
記する)樹脂からなる二軸延伸フイルムはその優
れた熱安定性、寸法安定性及び機械特性から各種
用途に使用されているが、特に磁気テープ用など
のベースフイルムとして、その有用性は周知であ
る。この用途ではベースフイルムの機械特性が良
好であるほど薄いフイルムを使用することが可能
となり、磁気テープ等の分野で機器を小型、軽量
化することができ、更に、同一寸法の機器におい
ては実質的な能力・容量の増大になる。 従来の二軸延伸PETフイルムでは従横両方向
ともF−5値(5%伸び時の張力)が10〜11Kg/
mm2であるが、これを改良するために縦・横二方向
に延伸した二軸延伸フイルムを更に縦方向に延伸
する所謂再縦延伸法がある。しかし、この方法で
は縦方向の機械特性の向上はなされるが、横方向
の機械特性は従来の二軸延伸PETフイルムと同
水準乃至やや低い。従つて、横方向の機械特性を
向上させるために再縦延伸後、再度横方向に再横
延伸する方法が提案されており(例えば特開昭50
−133276号公報、同55−22915号公報)、この方法
では確かに縦・横両方向とも機械特性が向上した
フイルムが得られる。しかし、この再縦延伸後に
再横延伸する方法は、通常の製造設備に較べて再
縦延伸工程、再横延伸工程、及び再熱固定固程が
必要なため非常に製造工程が長くなり、生産効率
が低く製造原価が増加し、しかも設備費が膨張す
るという欠点があつた。また別法として縦・横二
方向に延伸した二軸延伸フイルムを縦・横両方向
に同時に再延伸する方法が提案されている(例え
ば特開昭55−37305号公報、同55−27211号公報)
が、この方法でも製造工程が長くなり、更に同時
二軸延伸という複雑な延伸設備を使用しなければ
ならないという欠点があつた。本発明者はこのよ
うな欠点のない縦横両軸方向の機械強度の大きな
二軸延伸PETフイルムの製造方法について鋭意
研究した結果、再縦延伸及び再横延伸を必要とし
ない縦・横両方向とも機械特性の向上した二軸延
伸PETフイルムの製造方法を見い出し本発明に
到達した。 発明の目的 本発明の目的は縦・横両方向とも機械的強度、
ヤング率の高い二軸延伸PETフイルムを提供す
ることである。また別な目的は、比較的簡易な製
造設備により性能の優れたPETフイルムを製造
する技術を提供することにある。 発明の構成 本発明は、未延伸状態でかつ実質的に非晶状態
のフイルム状のPETを少くとも縦2段延伸し、
次いで横延伸し、更に熱固定を施すことからなる
二軸PETフイルムの製造方法である。 即ち、実質的に無定形のシート状PETを縦延
伸するにあたり、第一段目の縦延伸を120〜150℃
で降伏点倍率以上でかつ複屈折(△n)が0.005
〜0.025になるように延伸し、ひきつづき60〜110
℃で第二段目の縦延伸を行い、しかる後4.3倍以
上、好ましくは4.5倍以上、の倍率で横延伸し更
に、熱固定することからなる二軸延伸PETフイ
ルムの製造方法である。本発明を説明すると、本
発明でいうPETとはホモポリマーでも共重合体
(共重合体成分は好ましくは20%以下)でもよく、
またその分子量も通常のものを含む広範囲のもの
でよく、特に限定はない。更に、原料の段階で、
熱安定性、滑剤、紫外線吸収剤等の種々の添加剤
が含有されていてもよい。 次に本発明による二軸延伸PETフイルムの製
造方法を説明する。まず上記PETポリマーを十
分に乾燥した後、押出機により溶融押出し、フイ
ルター、口金を通して回転ドラム上にキヤストし
て急冷固化する。この急冷固化したフイルムは実
質的に非晶状態で低配向乃至未配向である。この
フイルムを120〜150℃の延伸温度において、降伏
点倍率以上で△nが0.005〜0.025になるように第
一段目縦延伸する。(以下この1段延伸された状
態をAフイルムと云う)。このとき延伸温度が120
℃より低いと得られる二軸延伸フイルムは縦方向
の機械特性(F−5値で代表)が低い。一方、
150℃以上では実質的にフロー延伸になつてしま
い延伸の効果が少なくなり、高温延伸に起因して
得られる二軸延伸フイルムの厚み斑が悪い。更に
延伸温度が120〜150℃の範囲内でも△nが0.005
未満では二軸延伸フイルムの縦方向のF−5値が
低く、0.025を超えると第2段目の縦延伸及びそ
の後の横延伸における作業性(延伸性)が低く、
特に横延伸において破断等のトラブルの発生頻度
が高くなる。120〜150℃で第1段目縦延伸する場
合、降伏点倍率以下で延伸すると、△nは0.005
以下になり、延伸倍率を降伏点倍率以上に選ぶ必
要がある。 次にAフイルムを60〜110℃、好ましくは70〜
100℃、更に好ましくは70〜90℃で第二段目の縦
延伸を行う(以下縦2段延伸を経た状態をBフイ
ルムと云う)。このBフイルムを得るとき、延伸
温度が低くすぎると延伸斑が発生したり、縦延伸
の操業性、安定性が損われたりし、延伸温度が高
すぎると延伸状態は安定するもののこの工程でB
フイルムに結晶化が著しく進行し、次の横延伸工
程で破断するなどのトラブルが頻発し安定生産出
来ない。これに対し、この第2段目の縦延伸にお
ける延伸倍率は、低くすぎると二軸延伸フイルム
の縦方向のF−5値が低く、厚み斑も悪い。また
延伸倍率が高すぎると後段の横延伸で破断が多発
し安定生産出来ないので、縦第2段では1.8〜3.0
倍が好適な延伸倍率である。 このようにして得られたBフイルムをステンタ
を用いて70〜120℃、好ましくは80〜100℃で4.3
倍以上、好ましくは4.5倍以上、の延伸倍率にお
いて横延伸し、次いで熱固定し巻き取る。横延伸
においては延伸温度が低くすぎると横延伸性が悪
化(破断発生)し、高すぎると厚み斑が悪くな
る。横延伸の延伸倍率においては、4.3倍以上に
しなければ横方向のF−5値が低い。 このように高温で一定の配向を与える縦延伸を
施し、その後ひきつづき同方向に比較的低温で第
2段縦延伸をし、更に横延伸・熱固定することに
より縦・横両方向に機械特性が向上した二軸延伸
PETフイルムが得られる理由は、高温の第1段
目縦延伸に加えて低温の第2段目縦延伸を施すと
いう2段目の縦延伸により、縦配向した構造を備
えているにも拘らず、Bフイルムは横延伸されや
すい緩和した構造が存在していて、その部分が優
先的に横延伸されると推測される。この結果、縦
延伸で造られた縦配向した構造がそのまゝ縦方向
に機械的な強度のような物性として発現されやす
いためと考えられる。 以下実施例と比較例を示し本発明を説明する。 実施例及び比較例1 実質的に無定形のシート状PETを縦延伸する
にあたり、第1段目の縦延伸を表−1に示すよう
な条件で行なつた。第2段目の縦延伸は延伸温度
を90℃にして延伸倍率は横延伸性が損なわれない
範囲で高くした条件で実施した。次いで横方向に
95℃で4.6倍延伸し210℃で熱固定し巻き取つた。
得られた二軸延伸フイルムのF−5値等を表−1
に示した。表−1に示されるように第1段目の縦
延伸温度の低いものや温度が適正でも△nが低く
すぎるものは縦方向のF−5値が低い。更に温度
が適正でも△nが高すぎると横延伸での破断が多
く安定製造出来ない。又温度が高すぎると二軸延
伸フイルムの厚み斑が悪く、実用に供し得ない。
Technical Field The present invention relates to a method for producing a biaxially oriented polyethylene terephthalate film, and more specifically to a biaxially oriented polyethylene terephthalate film that has improved mechanical properties in both longitudinal (longitudinal direction of the film) and transverse (width direction of the film) directions. This invention relates to a film manufacturing method. Prior art and its problems Biaxially stretched films made of polyethylene terephthalate (hereinafter abbreviated as PET) resin are used for various purposes due to their excellent thermal stability, dimensional stability, and mechanical properties, but in particular, they are used for magnetic tapes. Its usefulness as a base film is well known. In this application, the better the mechanical properties of the base film, the thinner the film can be used, making it possible to reduce the size and weight of equipment in fields such as magnetic tape. This will result in an increase in capacity and capacity. Conventional biaxially stretched PET film has an F-5 value (tension at 5% elongation) of 10 to 11 kg/
mm 2 , but in order to improve this, there is a so-called longitudinal re-stretching method in which a biaxially stretched film that has been stretched in both the longitudinal and transverse directions is further stretched in the longitudinal direction. However, although this method improves the mechanical properties in the longitudinal direction, the mechanical properties in the transverse direction are at the same level or slightly lower than those of conventional biaxially stretched PET films. Therefore, in order to improve the mechanical properties in the transverse direction, a method of re-stretching in the transverse direction after longitudinal re-stretching has been proposed (for example, in Japanese Patent Application Laid-Open No.
133276, 55-22915), this method certainly yields films with improved mechanical properties in both the longitudinal and lateral directions. However, this method of re-stretching horizontally after re-longitudinal stretching requires a re-longitudinal stretching process, a re-transverse stretching process, and a reheat-setting process compared to normal manufacturing equipment, making the manufacturing process extremely long. The drawbacks were low efficiency, increased manufacturing costs, and increased equipment costs. As another method, a method has been proposed in which a biaxially stretched film that has been stretched in both the vertical and horizontal directions is re-stretched in both the vertical and horizontal directions at the same time (for example, Japanese Patent Laid-Open Nos. 55-37305 and 55-27211).
However, this method also has disadvantages in that the manufacturing process is long and complicated stretching equipment for simultaneous biaxial stretching must be used. As a result of intensive research into a method for manufacturing a biaxially stretched PET film that does not have these drawbacks and has high mechanical strength in both longitudinal and transverse directions, the inventors of the present invention have developed a method for producing a biaxially stretched PET film that does not require re-stretching or re-stretching in both the longitudinal and transverse directions. The present invention was achieved by discovering a method for producing a biaxially stretched PET film with improved properties. Purpose of the invention The purpose of the present invention is to provide mechanical strength in both vertical and horizontal directions.
An object of the present invention is to provide a biaxially stretched PET film with a high Young's modulus. Another object is to provide a technique for manufacturing PET film with excellent performance using relatively simple manufacturing equipment. Structure of the Invention The present invention involves stretching a film-like PET in an unstretched state and a substantially amorphous state in at least two stages longitudinally,
This is a method for producing a biaxial PET film, which comprises then transverse stretching and further heat setting. That is, when longitudinally stretching substantially amorphous sheet-like PET, the first stage of longitudinal stretching is carried out at 120 to 150°C.
The yield point magnification is higher than that and the birefringence (△n) is 0.005.
Stretch to ~0.025 and continue to 60 to 110
This is a method for producing a biaxially stretched PET film, which comprises carrying out a second stage of longitudinal stretching at a temperature of 0.degree. To explain the present invention, PET as used in the present invention may be a homopolymer or a copolymer (the copolymer component is preferably 20% or less);
Moreover, its molecular weight may be in a wide range including ordinary ones, and is not particularly limited. Furthermore, at the raw material stage,
Various additives such as heat stabilizing agents, lubricants, ultraviolet absorbers, etc. may be contained. Next, a method for producing a biaxially stretched PET film according to the present invention will be explained. First, the PET polymer is sufficiently dried, then melt-extruded using an extruder, cast through a filter and a die onto a rotating drum, and rapidly cooled and solidified. This rapidly solidified film is substantially amorphous and poorly oriented to unoriented. This film is longitudinally stretched in the first stage at a stretching temperature of 120 to 150° C. at a yield point magnification or higher so that Δn is 0.005 to 0.025. (Hereinafter, this one-step stretched state will be referred to as A film). At this time, the stretching temperature was 120
When the temperature is lower than .degree. C., the biaxially stretched film obtained has low mechanical properties in the machine direction (represented by the F-5 value). on the other hand,
At 150° C. or higher, the stretching becomes substantially flow stretching, which reduces the stretching effect, and the obtained biaxially stretched film has poor thickness unevenness due to high temperature stretching. Furthermore, even if the stretching temperature is within the range of 120 to 150℃, △n is 0.005
If it is less than 0.025, the F-5 value in the longitudinal direction of the biaxially stretched film will be low, and if it exceeds 0.025, the workability (stretchability) in the second stage longitudinal stretching and subsequent transverse stretching will be low.
Particularly in transverse stretching, troubles such as breakage occur more frequently. When performing the first stage longitudinal stretching at 120 to 150°C, if the stretching is below the yield point magnification, △n is 0.005
The stretching ratio must be selected to be equal to or higher than the yield point ratio. Next, heat the A film at 60~110℃, preferably at 70~110℃.
A second stage of longitudinal stretching is carried out at 100°C, more preferably 70 to 90°C (hereinafter, the state after two stages of longitudinal stretching is referred to as a B film). When obtaining this B film, if the stretching temperature is too low, stretching unevenness will occur or the operability and stability of longitudinal stretching will be impaired; if the stretching temperature is too high, although the stretched state is stable, this step
Crystallization progresses significantly in the film, and troubles such as breakage occur frequently in the next horizontal stretching process, making stable production impossible. On the other hand, if the stretching ratio in the second stage of longitudinal stretching is too low, the F-5 value in the longitudinal direction of the biaxially stretched film will be low and the thickness will be uneven. In addition, if the stretching ratio is too high, breakage will occur frequently in the later stage of horizontal stretching, making stable production impossible.
A suitable stretching ratio is 200%. The thus obtained B film was heated to 70 to 120°C, preferably 80 to 100°C using a stenter for 4.3 hours.
The film is laterally stretched at a stretching ratio of at least 4.5 times, preferably at least 4.5 times, then heat set and rolled up. In transverse stretching, if the stretching temperature is too low, the transverse stretchability will deteriorate (occurrence of breakage), and if it is too high, thickness unevenness will worsen. The F-5 value in the lateral direction is low unless the stretching ratio for lateral stretching is 4.3 times or more. In this way, mechanical properties are improved in both the longitudinal and lateral directions by performing longitudinal stretching at a high temperature to give a constant orientation, followed by a second longitudinal stretching in the same direction at a relatively low temperature, and further transverse stretching and heat setting. biaxial stretching
The reason why PET film is obtained is that it has a longitudinally oriented structure due to the second stage of longitudinal stretching at a low temperature in addition to the first stage of longitudinal stretching at a high temperature. It is assumed that the B film has a relaxed structure that is easily horizontally stretched, and that this portion is preferentially horizontally stretched. As a result, it is thought that this is because the longitudinally oriented structure created by longitudinal stretching tends to exhibit physical properties such as mechanical strength in the longitudinal direction. The present invention will be explained below with reference to Examples and Comparative Examples. Examples and Comparative Example 1 When longitudinally stretching substantially amorphous sheet-like PET, the first stage of longitudinal stretching was carried out under the conditions shown in Table 1. The second stage of longitudinal stretching was carried out at a stretching temperature of 90°C and a stretching ratio as high as possible without impairing the transverse stretchability. then laterally
It was stretched 4.6 times at 95°C, heat-set at 210°C, and rolled up.
Table 1 shows the F-5 value of the obtained biaxially stretched film.
It was shown to. As shown in Table 1, the F-5 value in the longitudinal direction is low when the first stage longitudinal stretching temperature is low or when the temperature is appropriate but Δn is too low. Furthermore, even if the temperature is appropriate, if Δn is too high, there will be many breaks during lateral stretching, making stable production impossible. Furthermore, if the temperature is too high, the thickness of the biaxially stretched film will be poor and cannot be put to practical use.

【表】 実施例及び比較例2 実質的に無定形のシート状PETを縦延伸する
にあたり第1段目の縦延伸を140℃で2.5倍の条件
で行なつた。このフイルムの△nは0.0100であつ
た。このフイルムを表−2に示すような種々の温
度で第2段目の縦延伸をした。第2段目の縦延伸
倍率は横延伸性が損なわれない範囲で高くした条
件にし、次いで横方向に95℃で4.6倍延伸し210℃
で熱固定して巻き取つた。表−2に示されるよう
に第2段目縦延伸温度が50℃になると厚み斑が悪
化し、120℃ではF−5値が低く厚み斑も悪い。
[Table] Example and Comparative Example 2 In longitudinally stretching substantially amorphous sheet-like PET, the first stage of longitudinal stretching was carried out at 140° C. and at 2.5 times. The Δn of this film was 0.0100. This film was subjected to second stage longitudinal stretching at various temperatures as shown in Table 2. The longitudinal stretching ratio in the second stage was increased to the extent that the transverse stretchability was not impaired, and then the transverse direction was stretched 4.6 times at 95°C and then 210°C.
I heat-set it and rolled it up. As shown in Table 2, when the second stage longitudinal stretching temperature is 50°C, the thickness unevenness becomes worse, and at 120°C, the F-5 value is low and the thickness unevenness is also bad.

【表】 実施例及び比較例3 実質的に無定形のシート状PETを縦延伸する
にあたり、第1段目の縦延伸を140℃で2.5倍の条
件で行なつた。このフイルムの△nは0.0100であ
つた。このフイルムを90℃2.3倍の条件で第2段
目の縦延伸を行つた。次いで表−3に示した倍率
で横延伸した(温度は95℃)。熱固定は210℃で行
い巻取つた。表−3に示されるように横延伸倍率
が4.3倍未満であると横方向のF−5値が低くな
る。
[Table] Example and Comparative Example 3 When longitudinally stretching substantially amorphous sheet-like PET, the first stage of longitudinal stretching was carried out at 140° C. and at 2.5 times the stretching. The Δn of this film was 0.0100. This film was subjected to a second stage of longitudinal stretching at 90°C and 2.3 times the stretching temperature. Then, it was laterally stretched at the magnification shown in Table 3 (temperature: 95°C). The film was heat-set at 210°C and rolled up. As shown in Table 3, when the transverse stretching ratio is less than 4.3 times, the F-5 value in the transverse direction becomes low.

【表】 以上のように本発明によれば再縦延伸及び再横
延伸しなくても縦・横方向とも機械特性が向上し
た二軸延伸PETフイルムを製造することが出来
る。 発明の効果 本発明の製造方法によれば厚さ斑の少ないF−
5値の高い二軸延伸フイルムが得られる。本発明
は縦2段・横1段延伸によつて、従来の再縦・再
横延伸フイルムに匹敵する高い物性を備えた
PET二軸フイルムが得られる利点がある。
[Table] As described above, according to the present invention, a biaxially stretched PET film with improved mechanical properties in both the longitudinal and transverse directions can be produced without re-stretching in the longitudinal direction or in the transverse direction. Effects of the Invention According to the manufacturing method of the present invention, F-
A biaxially stretched film with a high 5 value can be obtained. The present invention achieves high physical properties comparable to conventional re-stretched and re-stretched films through two-stage longitudinal and one-stage transverse stretching.
There is an advantage that a PET biaxial film can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 実質的に非結晶状態のフイルム状ポリエチレ
ンテレフタレートを、120〜150℃の温度において
縦方向に降伏点倍率以上でかつ複屈折率が0.005
〜0.025となるように第1段目の縦延伸をなし、
ひきつづいて60〜110℃の温度において第2段目
の縦延伸を施し、しかる後横方向に4.3倍以上の
延伸倍率で横延伸し、更に熱固定を施すことから
なる二軸延伸ポリエチレンテレフタレートフイル
ムの製造方法。
1 Film-like polyethylene terephthalate in a substantially amorphous state has a yield point magnification in the longitudinal direction at a temperature of 120 to 150°C and a birefringence of 0.005.
The first stage of longitudinal stretching is carried out so that it becomes ~0.025,
A biaxially stretched polyethylene terephthalate film which is then subjected to a second stage of longitudinal stretching at a temperature of 60 to 110°C, then laterally stretched in the transverse direction at a stretching ratio of 4.3 times or more, and further heat-set. Production method.
JP8140985A 1985-04-18 1985-04-18 Manufacture of biaxially oriented polyethylene terephthalate film Granted JPS61241128A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8140985A JPS61241128A (en) 1985-04-18 1985-04-18 Manufacture of biaxially oriented polyethylene terephthalate film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8140985A JPS61241128A (en) 1985-04-18 1985-04-18 Manufacture of biaxially oriented polyethylene terephthalate film

Publications (2)

Publication Number Publication Date
JPS61241128A JPS61241128A (en) 1986-10-27
JPH04455B2 true JPH04455B2 (en) 1992-01-07

Family

ID=13745533

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8140985A Granted JPS61241128A (en) 1985-04-18 1985-04-18 Manufacture of biaxially oriented polyethylene terephthalate film

Country Status (1)

Country Link
JP (1) JPS61241128A (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS498514A (en) * 1972-05-13 1974-01-25
JPS4922945A (en) * 1972-06-20 1974-02-28
JPS5878729A (en) * 1981-11-04 1983-05-12 Diafoil Co Ltd Preparation of biaxially-oriented polyester film
JPS60176743A (en) * 1984-02-23 1985-09-10 Diafoil Co Ltd Manufacture of biaxially oriented polyester film

Also Published As

Publication number Publication date
JPS61241128A (en) 1986-10-27

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