JPH07178810A - Biaxially oriented polyester film roll - Google Patents
Biaxially oriented polyester film rollInfo
- Publication number
- JPH07178810A JPH07178810A JP32416693A JP32416693A JPH07178810A JP H07178810 A JPH07178810 A JP H07178810A JP 32416693 A JP32416693 A JP 32416693A JP 32416693 A JP32416693 A JP 32416693A JP H07178810 A JPH07178810 A JP H07178810A
- Authority
- JP
- Japan
- Prior art keywords
- film
- elongation
- tma
- film roll
- difference
- 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
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、フィルムの加工工程に
おける蛇行や片寄りがなく、加工安定性に優れた二軸配
向ポリエステルフイルムロールに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biaxially oriented polyester film roll which is free from meandering or deviation in the film processing step and is excellent in processing stability.
【0002】[0002]
【従来の技術】磁気テープや粘着テープ、印刷品、電気
絶縁品、写真受像ベースなどの各種用途において、その
寸法安定性の理由から二軸配向ポリエステルフイルムが
多く使われている。しかしながら、二軸配向ポリエステ
ルフイルムロールには幅方向の特性むらがあり、このた
めフィルムの加工工程において蛇行や片寄りを生じて、
塗布むら、しわといった品質の不安定な加工製品を引き
起こしていた。特に、その二軸配向ポリエステルフイル
ムロールの幅が広い程不安定であり、また、二軸配向ポ
リエステルフイルム製造のエッヂに近い部分、つまり長
手方向に対する主配向方向が5〜85°のフィルムロー
ルがより不安定であった。かかる蛇行や片寄りの改良の
試みとして例えば特開昭55−95517が提案され、
また、幅方向の特性むらの改良の試みとして例えば特公
昭63−36972が提案されてきたが、蛇行や片寄り
を引き起こす幅方向の特性むらの本質が解明できず十分
な改良に至っていなかった。2. Description of the Related Art Biaxially oriented polyester films are widely used in various applications such as magnetic tapes, adhesive tapes, printed products, electrical insulating products, and photographic image receiving bases because of their dimensional stability. However, the biaxially oriented polyester film roll has characteristic unevenness in the width direction, which causes meandering or deviation in the film processing step,
It caused processed products of unstable quality such as uneven coating and wrinkles. In particular, the wider the width of the biaxially oriented polyester film roll is, the more unstable it is. Further, the part close to the edge of the production of the biaxially oriented polyester film, that is, the film roll having a main orientation direction of 5 to 85 ° with respect to the longitudinal direction is more preferable. It was unstable. For example, JP-A-55-95517 has been proposed as an attempt to improve such meandering and deviation.
Further, as an attempt to improve the characteristic unevenness in the width direction, for example, Japanese Examined Patent Publication No. Sho 63-36972 has been proposed, but the essence of the characteristic unevenness in the width direction which causes meandering or deviation has not been elucidated and it has not been sufficiently improved. .
【0003】[0003]
【発明が解決しようとする課題】本発明は、この幅方向
の特性むらの本質を解明し、フィルムの加工工程におけ
る蛇行や片寄りがなく、加工安定性に優れた二軸配向ポ
リエステルフイルムロールを提供することを目的とす
る。The present invention has clarified the essence of this characteristic unevenness in the width direction, and has a biaxially oriented polyester film roll which is free from meandering and unevenness in the film processing step and has excellent processing stability. The purpose is to provide.
【0004】[0004]
【課題を解決するための手段】この目的に沿う本発明の
二軸配向ポリエステルフイルムロールは、100℃にお
けるTMA伸びが0.001%以上であって、かつ、1
00℃におけるTMA伸びの両サイドの差が0.1%以
下のものから成る。The biaxially oriented polyester film roll of the present invention which meets this object has a TMA elongation at 100 ° C. of 0.001% or more, and
It is composed of a material having a difference of 0.1% or less on both sides of TMA elongation at 00 ° C.
【0005】本発明における二軸配向ポリエステルフイ
ルムとは、縦、横に延伸配向されたフィルムであって、
ポリエチレンテレフタレート、ポリブチレンテレフタレ
ート、ポリエチレンナフタレートで代表されるポリエス
テルフイルムあるいはこれらの共重合体のポリエステル
フイルムをいう。あるいはこれらの積層フイルム、強力
化フイルムであっても良い。フィルムの中には、ポリエ
ステル重合時に作られる内部析出粒子や炭酸カルシウ
ム、酸化アルミニウム、酸化ケイ素、酸化チタン等に代
表される不活性無機粒子あるいは有機粒子を含んでいて
も良い。The biaxially oriented polyester film in the present invention is a film stretched and oriented in the longitudinal and transverse directions,
A polyester film represented by polyethylene terephthalate, polybutylene terephthalate, polyethylene naphthalate or a polyester film of a copolymer thereof. Alternatively, a laminated film or a strengthened film of these may be used. The film may contain internally precipitated particles produced during polyester polymerization and inert inorganic particles or organic particles represented by calcium carbonate, aluminum oxide, silicon oxide, titanium oxide and the like.
【0006】本発明の二軸配向ポリエステルフイルムロ
ールは、100℃におけるTMA伸びが0.001%以
上であって、かつ、100℃におけるTMA伸びの両サ
イドの差が0.1%以下であることが必要である。TM
A伸びとは、以下に示す方法で測定した値であって、従
来、幅方向の特性むらとして提言されてきた片伸び、熱
寸法変化、結晶化度などとは異なり、昇温速度、温度、
時間、張力などフィルムの加工工程における特性むらの
本質を表すものであり、鋭意検討の結果、本発明に至っ
た。The biaxially oriented polyester film roll of the present invention has a TMA elongation at 100 ° C. of not less than 0.001% and a difference between the two sides of TMA elongation at 100 ° C. of not more than 0.1%. is necessary. TM
The A elongation is a value measured by the method described below, and is different from the one-sided elongation, the thermal dimensional change, the crystallinity, etc. which have been conventionally proposed as the characteristic unevenness in the width direction, and the temperature rising rate, the temperature,
It represents the essence of characteristic unevenness in the film processing process such as time and tension, and as a result of intensive studies, the present invention has been accomplished.
【0007】TMA伸びが0.001%より小さいかま
たは縮みであれば、フィルムの加工工程で引きつれやし
わを生じるので好ましくない。TMA伸びのより好まし
い範囲は0.005%〜0.3%、さらに好ましい範囲
は0.01%〜0.2%である。If the TMA elongation is less than 0.001% or shrinks, it is not preferable because it causes tears and wrinkles in the film processing step. A more preferable range of TMA elongation is 0.005% to 0.3%, and a further preferable range is 0.01% to 0.2%.
【0008】また、100℃におけるTMA伸びの両サ
イドの差が0.1%より大きければ、フィルムの加工工
程で蛇行したり片寄りしたりして、好ましくない。TM
A伸びの差のより好ましい範囲は、0.0%〜0.05
%、さらに好ましい範囲は0.0%〜0.02%であ
る。If the difference between the two sides of TMA elongation at 100 ° C. is larger than 0.1%, the film will be meandered or offset in the film processing step, which is not preferable. TM
A more preferable range of the difference in A elongation is 0.0% to 0.05.
%, And a more preferable range is 0.0% to 0.02%.
【0009】本発明は、その幅が0.3m以上、より好
ましくは0.6m以上のフィルムロールに特に有効であ
る。幅が小さい場合には、フィルムの加工工程における
張力が幅方向の特性むらに打ち勝ってフィルムの加工工
程における蛇行や片寄りが少なくなり、本発明の有効性
が小さくなる傾向にある。The present invention is particularly effective for a film roll having a width of 0.3 m or more, more preferably 0.6 m or more. When the width is small, the tension in the film processing step overcomes the characteristic unevenness in the width direction, and the meandering or deviation in the film processing step is reduced, which tends to reduce the effectiveness of the present invention.
【0010】また本発明は、フイルム製造の際にエッヂ
に近い部分、つまり少なくとも一方の端部における長手
方向に対する主配向方向が5°〜85°、より好ましく
は8°〜82°の範囲にあるフィルムロールの場合に特
に有効である。Further, according to the present invention, the main orientation direction with respect to the longitudinal direction at a portion close to the edge, that is, at least one end portion in the film production is in the range of 5 ° to 85 °, more preferably 8 ° to 82 °. It is particularly effective in the case of a film roll.
【0011】本発明では、フィルムの片伸び値は、10
mm以下が好ましく、より好ましくは0mm〜8mmで
ある。この値が大きいと、フィルムの加工工程における
蛇行が大きくなる傾向にある。In the present invention, the elongation value of the film is 10
mm or less, and more preferably 0 mm to 8 mm. When this value is large, the meandering in the film processing step tends to increase.
【0012】また、本発明では、フィルムの長手方向の
80℃、30分での熱収縮率は、0.3%以下が好まし
く、より好ましくは0.25%〜−0.05%である。
この値が大きいと、フィルムの引きつれが大きくなる傾
向にある。In the present invention, the heat shrinkage ratio of the film in the longitudinal direction at 80 ° C. for 30 minutes is preferably 0.3% or less, more preferably 0.25% to −0.05%.
When this value is large, there is a tendency that film tearing becomes large.
【0013】つぎに本発明の製造方法について説明する
が、これに限定されるものではない。ポリエチレンテレ
フタレート等のポリエステル原料を押出機で溶融押出し
て冷却し、これを縦、横に延伸する。倍率は縦に3.0
〜6.0倍、横に3.2〜4.5が通常で、更にこれを
再縦延伸、再横延伸しても良い。この後、テンターで熱
処理し、クリップオフした後、縦にリラックスする。こ
の際、クリップが把持していたエッジの温度を140℃
以下、エッジを除いたフィルムの温度は130℃以下、
かつエッジとフィルムの温度差を50℃以内にしておく
のが良い。この後常温に冷却して、エッジを取り除き、
巻取り、さらにスリットし、コアに巻取して、二軸配向
ポリエステルフイルムロールとする。リラックス率は
0.01%〜3.0%とするのが通常である。あるい
は、TMA伸びが0.01%より小さいフイルムロール
を、一旦加熱オブーンにいれて張力をかける方法や、T
MA伸びの差が0.1%より大きいフイルムロールを、
一旦加熱オブーンにいれて低張力で加熱する方法も取る
ことができる。Next, the manufacturing method of the present invention will be explained, but the present invention is not limited to this. A polyester raw material such as polyethylene terephthalate is melt-extruded with an extruder and cooled, and this is stretched lengthwise and widthwise. Magnification is 3.0 vertically
It is usually 6.0 times, and 3.2 to 4.5 in the horizontal direction, and this may be further longitudinally stretched and laterally stretched. After this, heat treat with a tenter, clip off, and then relax vertically. At this time, the temperature of the edge gripped by the clip is 140 ° C.
Below, the temperature of the film excluding the edges is 130 ° C or less,
In addition, the temperature difference between the edge and the film is preferably kept within 50 ° C. Then cool to room temperature to remove the edges,
It is wound up, slitted, and wound up on a core to obtain a biaxially oriented polyester film roll. The relaxation rate is usually 0.01% to 3.0%. Alternatively, a film roll having a TMA elongation of less than 0.01% is once placed in a heating oven to apply tension, or
A film roll with a difference in MA elongation of more than 0.1%,
It is also possible to take a method of once putting in a heating oven and heating with low tension.
【0014】[0014]
【物性の測定方法ならびに効果の評価方法】測定方法、
評価方法について説明する。[Measurement method of physical properties and evaluation method of effect] Measurement method,
The evaluation method will be described.
【0015】1.TMA伸び 幅5mm、長さ20mmのサンプルに30gの荷重をか
けて、常温から30℃/分の昇温速度で加熱し、100
℃到達時の寸法伸びを読む。測定器としては、例えば真
空理工(株)製のTM7000などが使用できる。フィ
ルムロールの両サイドの平均をとった。1. TMA elongation A sample having a width of 5 mm and a length of 20 mm is loaded with a load of 30 g and heated at a temperature rising rate of 30 ° C./minute from room temperature to 100.
Read the dimensional elongation when reaching ℃. As the measuring device, for example, TM7000 manufactured by Vacuum Riko Co., Ltd. can be used. The average of both sides of the film roll was taken.
【0016】2.TMA伸びの差 フィルムロールの両端からそれぞれ50mm以内の部分
からサンプルを取り、両サンプルのTMA伸びをそれぞ
れ測定し、両者の差をTMA伸びの差とする。 3.主配向方向 アッベの屈折計で測定した屈折率がフィルム面内で最大
となる方向とした。2. Difference in TMA Elongation Samples are taken from portions within 50 mm from both ends of the film roll, the TMA elongations of both samples are measured, and the difference between the two is taken as the difference in TMA elongation. 3. Main orientation direction The direction in which the refractive index measured by Abbe's refractometer was the maximum in the film plane.
【0017】4.フィルムの片伸び値 図1のように、フィルムロールからフィルム10mを取
り出して、平板上におき、フィルムと平板の間の空気を
取り除いた後、フィルム10mの端から端に糸をはり、
中央5m部のフィルムと糸の距離d(mm)をフィルム
の片伸び値とした。4. Single-elongation value of film As shown in FIG. 1, the film 10m was taken out from the film roll, placed on a flat plate, air between the film and the flat plate was removed, and then a thread was wound from end to end of the film 10m,
The distance d (mm) between the film and the thread at the center of 5 m was taken as the half-stretch value of the film.
【0018】5.熱収縮率 フィルムの長手方向に長さ20cm、幅10mmに切っ
たサンプルを、80℃の熱風オーブンに30分間放置し
た後、取り出して常温にもどし、その加熱前後の寸法変
化から熱収縮率を求めた。5. Heat Shrinkage A sample cut into a length of 20 cm and a width of 10 mm in the longitudinal direction of the film was left in a hot air oven at 80 ° C. for 30 minutes, then taken out and returned to room temperature, and the heat shrinkage was calculated from the dimensional change before and after heating. It was
【0019】6.フィルムの蛇行 フイルムロールをコータにかけて塗布を開始してから、
コータに対するフィルムの位置のずれを蛇行とした。6. After applying the meandering film roll of the film to the coater to start coating,
The deviation of the position of the film with respect to the coater was meandering.
【0020】7.塗布むら、しわ 塗布したフィルムに上下から蛍光灯を当てて、その反射
光、透過光から肉眼により塗布むら、しわの有無を観察
した。7. Coating unevenness and wrinkles A fluorescent lamp was applied to the coated film from above and below, and the presence or absence of coating unevenness and wrinkles was visually observed from the reflected light and transmitted light.
【0021】[0021]
実施例1 ポリエチレンテレフタレート樹脂を押出機で280℃に
溶融、押出して25℃に冷却して160μmの未延伸フ
ィルムを得た。これを縦に3.3倍、横に3.8倍延伸
し、更に縦に1.5倍延伸し、テンターで200℃で5
秒間熱処理した後、クリップオフした後、縦に0.3%
リラックスした。フィルムの温度は90℃、クリップエ
ッジ部分の温度を110℃にした。この後常温に冷却し
て、エッジを取り除き、巻取って厚みが8μで幅350
0mmのフィルムを得た。これを4分割にスリットし
て、端のフィルムをコアに10000m巻取して、幅が
800mmの二軸配向ポリエステルフイルムロールを得
た。このロールのエッジに近い側のサイドにおける長手
方向に対する主配向方向は25゜であった。フイルムロ
ールの100℃におけるTMA伸びは、エッジに近い側
のサイドが0.03%、もう一方のサイドが0.035
%であり、両サイドの100℃におけるTMA伸びの差
が0.005%であった。また、フィルムの片伸び値
は、3mmで、フィルムの長手方向の80℃30分の熱
収縮率は、0.2%であった。このフイルムロールをコ
ータにかけて、濃度20%の磁気テープ塗液を5μm塗
布し、110℃に加熱して乾燥したが、フイルムの蛇行
は1mm以下で、塗布むらやしわのない加工製品が得ら
れた。Example 1 A polyethylene terephthalate resin was melted at 280 ° C. with an extruder, extruded and cooled to 25 ° C. to obtain an unstretched film of 160 μm. This was stretched 3.3 times in the lengthwise direction and 3.8 times in the width direction, and further stretched 1.5 times in the lengthwise direction.
After heat treatment for 2 seconds, after clipping off, 0.3% vertically
relaxed. The temperature of the film was 90 ° C., and the temperature of the clip edge portion was 110 ° C. After that, it is cooled to room temperature, the edges are removed, and it is rolled up to have a thickness of 8 μ and a width of 350 μm.
A 0 mm film was obtained. This was slit into 4 sections and the film at the end was wound around a core for 10000 m to obtain a biaxially oriented polyester film roll having a width of 800 mm. The main orientation direction with respect to the longitudinal direction on the side near the edge of this roll was 25 °. The TMA elongation of the film roll at 100 ° C. is 0.03% on the side close to the edge and 0.035% on the other side.
%, And the difference in TMA elongation at 100 ° C. on both sides was 0.005%. The single elongation value of the film was 3 mm, and the heat shrinkage ratio of the film in the longitudinal direction at 80 ° C. for 30 minutes was 0.2%. A magnetic tape coating liquid having a concentration of 20% was applied to a thickness of 5 μm on a coater using this film roll, and the coating was heated to 110 ° C. and dried. .
【0022】比較例1 縦のリラックスを0.1%にし、クリップエッジ部分の
温度を160℃にしたほかは、実施例1と同様にして幅
が800mmの二軸配向ポリエステルフイルムロールを
得た。このロールのエッジに近い側のサイドにおける長
手方向に対する主配向方向は25゜であった。フイルム
ロールの100℃におけるTMA伸びは、エッジに近い
側のサイドが0.07%、もう一方のサイドが−0.0
8%であり、両サイドの100℃におけるTMA伸びの
差が0.15%であった。また、フィルムの片伸び値は
17mmで、フィルムの長手方向の80℃30分の熱収
縮率は0.4%であった。このフイルムロールをコータ
にかけて、濃度20%の磁気テープ塗液を5μm塗布
し、110℃に加熱して乾燥したところ、フイルムが5
5mm蛇行して塗膜が片寄りし、塗布むらとしわの多い
加工製品となった。Comparative Example 1 A biaxially oriented polyester film roll having a width of 800 mm was obtained in the same manner as in Example 1 except that the longitudinal relaxation was set to 0.1% and the temperature of the clip edge portion was set to 160 ° C. The main orientation direction with respect to the longitudinal direction on the side near the edge of this roll was 25 °. The TMA elongation at 100 ° C. of the film roll is 0.07% on the side close to the edge and −0.0 on the other side.
8%, and the difference in TMA elongation at 100 ° C. on both sides was 0.15%. The single-sided elongation value of the film was 17 mm, and the heat shrinkage ratio of the film in the longitudinal direction at 80 ° C. for 30 minutes was 0.4%. The film roll was coated on a coater with a magnetic tape coating solution having a concentration of 20% by 5 μm, and the film was heated to 110 ° C. and dried.
The coating film deviated by 5 mm meandering, resulting in a processed product with uneven coating and wrinkles.
【0023】実施例2 比較例1で得られた幅が800mmの二軸配向ポリエス
テルフイルムロールを、100℃の加熱オブーンにいれ
て5kg/mの張力で5秒間加熱し巻き取った。このロ
ールのエッジに近い側のサイドにおける長手方向に対す
る主配向方向は25゜であった。フイルムロールの10
0℃におけるTMA伸びは、エッジに近い側のサイドが
0.05%、もう一方のサイドが0.03%であり、両
サイドの100℃におけるTMA伸びの差が0.02%
であった。また、フィルムの片伸び値は5mmで、フィ
ルムの長手方向の80℃30分の熱収縮率は0.1%で
あった。このフイルムロールをコータにかけて、濃度2
0%の磁気テープ塗液を5μ塗布し、110℃に加熱し
て乾燥したが、フイルムの蛇行は3mm以下で、塗布む
らやしわのない加工製品が得られた。Example 2 The biaxially oriented polyester film roll having a width of 800 mm obtained in Comparative Example 1 was placed in a heating oven at 100 ° C. and heated at a tension of 5 kg / m for 5 seconds and wound up. The main orientation direction with respect to the longitudinal direction on the side near the edge of this roll was 25 °. Film roll 10
The TMA elongation at 0 ° C is 0.05% on the side close to the edge and 0.03% on the other side, and the difference in TMA elongation at 100 ° C on both sides is 0.02%.
Met. Moreover, the single-elongation value of the film was 5 mm, and the heat shrinkage ratio of the film in the longitudinal direction at 80 ° C. for 30 minutes was 0.1%. Apply this film roll to a coater to get a density of 2
5 μ of 0% magnetic tape coating liquid was applied, and the film was heated to 110 ° C. and dried, but the film meandering was 3 mm or less, and a processed product without coating unevenness and wrinkles was obtained.
【0024】[0024]
【発明の効果】 100℃におけるTMA伸びの値を大
きくし、両サイドの差を小さくすることによって、コー
ティング、乾燥、張合わせ、蒸着、巻取といったフィル
ムの加工工程でのフィルムの蛇行や片寄りが無くなり、
安定した加工製品が得られた。EFFECTS OF THE INVENTION By increasing the value of TMA elongation at 100 ° C. and decreasing the difference between both sides, the meandering and deviation of the film in the film processing steps such as coating, drying, laminating, vapor deposition and winding. Disappeared,
A stable processed product was obtained.
【図1】 フィルムの片伸び値の測定方法を示す。FIG. 1 shows a method for measuring a piece elongation value of a film.
1.フィルム 2.糸 1. Film 2. yarn
Claims (3)
1%以上であって、かつ、100℃におけるTMA伸び
の両サイドの差が0.1%以下であることを特徴とする
二軸配向ポリエステルフイルムロール。1. The TMA elongation at 100 ° C. is 0.00.
A biaxially oriented polyester film roll, which is 1% or more and has a difference of 0.1% or less on both sides of TMA elongation at 100 ° C.
って、少なくとも一方の端部における長手方向に対する
主配向方向が5°〜85°である請求項1に記載の二軸
配向ポリエステルフイルムロール。2. The biaxially oriented polyester film roll according to claim 1, wherein the width of the film roll is 0.3 m or more, and the main orientation direction with respect to the longitudinal direction at at least one end is 5 ° to 85 °. .
ある請求項1または2に記載の二軸配向ポリエステルフ
イルムロール。3. The biaxially oriented polyester film roll according to claim 1, wherein the film has a single elongation value of 10 mm or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32416693A JPH07178810A (en) | 1993-12-22 | 1993-12-22 | Biaxially oriented polyester film roll |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32416693A JPH07178810A (en) | 1993-12-22 | 1993-12-22 | Biaxially oriented polyester film roll |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07178810A true JPH07178810A (en) | 1995-07-18 |
Family
ID=18162845
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32416693A Pending JPH07178810A (en) | 1993-12-22 | 1993-12-22 | Biaxially oriented polyester film roll |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07178810A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014195985A (en) * | 2013-03-08 | 2014-10-16 | 東レ株式会社 | Biaxially oriented polyester film and method for manufacturing the same |
-
1993
- 1993-12-22 JP JP32416693A patent/JPH07178810A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014195985A (en) * | 2013-03-08 | 2014-10-16 | 東レ株式会社 | Biaxially oriented polyester film and method for manufacturing the same |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1920902A1 (en) | Process for production of biaxially oriented polyester film | |
KR960013068B1 (en) | Thermoplastic resin film & a method for producing the same | |
JPS61211014A (en) | Biaxial oriented heat-set film having improved abrasion resistance consisting of thermoplastic polyester | |
JPH0617065B2 (en) | Heat treatment method for biaxially stretched polyester film | |
JPH07178810A (en) | Biaxially oriented polyester film roll | |
JP2505474B2 (en) | Easy folding polyester film | |
JPS6321603B2 (en) | ||
JPH0125694B2 (en) | ||
JPS63104822A (en) | Biaxially oriented polyethylene terephthalate film | |
KR0158241B1 (en) | Process for preparing polyester film | |
JPS6243857B2 (en) | ||
JPS5878729A (en) | Preparation of biaxially-oriented polyester film | |
JPH0117857B2 (en) | ||
JPH03284934A (en) | Manufacture of biaxially oriented polyester film | |
JPH0643097B2 (en) | Method for producing biaxially oriented polyester film | |
JPH0459332A (en) | Thermoplastic resin film and its manufacture | |
EP0960718A1 (en) | Biaxially oriented polyester film | |
JPH01165423A (en) | Preparation of biaxially oriented polyester film | |
JPS59114028A (en) | Manufacture of thermoplastic resin film | |
JPH0243022A (en) | Biaxially-oriented polyethylene terephthalate film | |
JPH06254959A (en) | Biaxially stretched polyester film for mold lubrication | |
JP2589547B2 (en) | Method for producing biaxially oriented polyester film for magnetic recording medium | |
JP2003019748A (en) | Manufacturing method for thermoplastic resin film | |
JPH03161319A (en) | Manufacture of biaxially-oriented polyester film | |
JP2555707B2 (en) | Process for producing polyethylene 2,6-naphthalate film |