JPS61233523A - Preparation of biaxially oriented polyester film - Google Patents

Preparation of biaxially oriented polyester film

Info

Publication number
JPS61233523A
JPS61233523A JP7353185A JP7353185A JPS61233523A JP S61233523 A JPS61233523 A JP S61233523A JP 7353185 A JP7353185 A JP 7353185A JP 7353185 A JP7353185 A JP 7353185A JP S61233523 A JPS61233523 A JP S61233523A
Authority
JP
Japan
Prior art keywords
film
heating
tension
zone
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.)
Pending
Application number
JP7353185A
Other languages
Japanese (ja)
Inventor
Iemi Satake
佐竹 舎巳
Hiroshi Hatakeyama
博 畠山
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.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film 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 Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP7353185A priority Critical patent/JPS61233523A/en
Publication of JPS61233523A publication Critical patent/JPS61233523A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To improve dimensional stability and flatness, by setting the tension of a polyester film after the completion of biaxial orientation in the longitudinal direction of said film to a specific value or less and heating the central part and side edge parts of the film to specific temps. to hold said temps. CONSTITUTION:A film 4 after the completion of biaxial orientation is sent into a heat treatment apparatus and successively passed through a heating zone 1, a cooling zone 2 and a tension separation zone 3 to be taken up. As a heating means, an infrared heater is used and the temp. of the central part of the film is heated to 150 deg.C or more while each of the side edge parts of said film is heated to temp. 10 deg.C more higher than that of the central part. In order to make a heat shrinkage value sufficiently low in the longitudinal direction by heat treatment, the tension of the film in the longitudinal direction within the heating zone 1 is set to 10kg/m or less. After heating, the film is gradually cooled in the cooling zone 2 to eliminate the strain generated by heat treatment. The cooled film is released from tension and taken up on and after under proper tension.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、例えば写真フィルムベース、磁気テープベー
スなどに利用される二軸延伸ポリエステルフィルムの製
造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing a biaxially oriented polyester film used, for example, in photographic film bases, magnetic tape bases, and the like.

(従来の技術) ポリエステルフィルムを二軸延伸しただけでは寸法安定
性が悪いところからこれをさらに熱処理することが通常
行なわれている。一般的な熱処理は熱風による加熱ゾー
ンと冷却ゾーンを通過させることにより行なわれていた
。しかし、この方法では寸法安定性の改良が不充分なば
かシでなく、中たるみ、耳のび、ベンディングなどを生
じてフィルムの平面性が損なわれるという問題もあった
(Prior Art) Since dimensional stability is poor when a polyester film is only biaxially stretched, it is usually further heat-treated. Conventional heat treatment was performed by passing hot air through a heating zone and a cooling zone. However, this method not only does not improve dimensional stability sufficiently, but also has the problem of causing sagging, sagging, bending, etc., which impairs the flatness of the film.

ここで言うベンディングとは、遂次二軸延伸を行なう際
、テンター内での収縮応力が中央部に集中するため生じ
るベース長手方向の曲がりを示すものであり、テンター
巾(食中)ベースを半裁すると顕著になるものである。
Bending here refers to the bending in the longitudinal direction of the base that occurs when shrinkage stress in the tenter is concentrated in the center during successive biaxial stretching, and the bending occurs when the base is cut in half by the width of the tenter. Then it becomes noticeable.

そこで、このような問題を解決するべく各所で研究が行
なわれ、次のような方法が提案されている。
Therefore, research is being conducted in various places to solve such problems, and the following methods have been proposed.

まず、特開昭!r−71132参号公報には、二軸延伸
フィルムをロール間で熱処理を施す際に、その温度、張
力及び時間を特定範囲内とすることによって寸法安定性
及び平面性を改善することが開示されている。
First, Tokukai Akira! Publication R-71132 discloses that when a biaxially stretched film is heat treated between rolls, the dimensional stability and flatness are improved by controlling the temperature, tension and time within a specific range. ing.

また、特開昭33−2407−号公報には、二軸延伸し
たフィルムをその幅方向に制限収縮を与えながら熱固定
し、次いで加圧空気でフィルムを保持しつつ低張力で馳
緩熱処理を行なうことによって寸法安定性を改善する方
法が開示されている。
Furthermore, Japanese Patent Application Laid-open No. 33-2407 discloses that a biaxially stretched film is heat-set while giving limited shrinkage in the width direction, and then subjected to slow heat treatment under low tension while holding the film with pressurized air. A method is disclosed for improving dimensional stability by:

さらに、特開昭17−/jり27号公報には、二軸延伸
されかつ熱固定されたフィルムに対して1その長手方向
を低張力にして、熱風を吹き付けて支持しつつl仏0−
/r℃cの温度で3〜/j秒間加熱することによって寸
法安定性を改善する方法が開示されている。
Furthermore, Japanese Patent Application Laid-Open No. 17-17-27 discloses that a biaxially stretched and heat-set film is placed under low tension in its longitudinal direction, and supported by blowing hot air.
A method is disclosed for improving dimensional stability by heating at a temperature of /r°C for 3 to /j seconds.

そのほか、特公昭jlr−3!/JJ−号公報には、ポ
リエステルフィルムを空気の吹き付けによって支持させ
て搬送するとともに、該フィルムを二次転移点以上の温
度で加熱して軟化後、これを湾曲状態で二次転移点以下
の温度で冷却、硬化させることにより平面性を改善する
方法が開示されている。
In addition, Tokko Sho JLR-3! /JJ- Publication discloses that a polyester film is supported and conveyed by air blowing, the film is heated to a temperature higher than the secondary transition point to soften it, and then the film is bent in a curved state to a temperature lower than the secondary transition point. A method of improving flatness by cooling and curing at a temperature is disclosed.

(発明が解決しようとする問題点) 本発明者らの検討によれば、特開昭!r−7≠32参号
公報の方法号公報には特に平面性の改良に限界があって
中だるみ、耳のび等の発生にまだ問題があり、また、ベ
ンディングの問題も残っていた。
(Problems to be Solved by the Invention) According to the studies of the present inventors, JP-A-Sho! The method disclosed in Publication No. r-7≠32 has limitations in improving the flatness, and there are still problems with the occurrence of sagging in the middle, stretch of the edges, etc., and the problem of bending still remains.

特開昭j3−タ1,072号公報、特開昭37−7!タ
一フ号公報及び特公昭ll−3113j号公報に開示さ
れている各方法においては、いずれもエアー搬送方式が
採用されているために設備が大がかりになるという問題
があった。
JP-A No. 1,072, JP-A No. 37-7! Each of the methods disclosed in Japanese Patent Publication No. 1F and Japanese Patent Publication No. 3113J has a problem in that the equipment becomes large-scale because they both use an air conveyance system.

さらに、熱風による加熱の場合には長大な加熱ゾーンが
必要になるという問題があった。また、加熱及び冷却の
際に温度ムラを生じて平面性を阻害することが多く、こ
れを防止するために徐冷化また冷却風の巾方向分布等の
考慮等の必要があって冷却ゾーンも長大なものになって
いた。
Furthermore, heating with hot air requires a long heating zone. In addition, temperature unevenness often occurs during heating and cooling, which impairs flatness, and to prevent this, it is necessary to slow cooling and consider the widthwise distribution of cooling air, etc. It had become a long one.

赤外線ヒーターによる加熱方式も知られていたが(%開
閉!3−2407λ号公報)、均一加熱が難しい等の理
由で採用されるに至っていなかった。
Although a heating method using an infrared heater was known (%Open/Close! Publication No. 3-2407λ), it had not been adopted due to the difficulty of uniform heating.

(問題点を解決するための手段) 本発明は、これらの問題点を解決するべくなされたもの
であり、赤外線ヒーターを利用してフィルムの幅方向に
温度分布をもたせて加熱するようにしたことを特徴とし
ている。
(Means for Solving the Problems) The present invention has been made to solve these problems, and includes heating the film with a temperature distribution in the width direction using an infrared heater. It is characterized by

すなわち、本発明は、ポリエステルフィルムを、二軸延
伸終了後、フィルム長手方向の張力を10Kg/m以下
とし、赤外線ヒーターにより該フィルム中央部の温度が
1zo0c以上であって側縁部の温度が該中央部の温度
よりもIO’C以上高くなるようにして3秒以上加熱す
ることを特徴とする二軸延伸ポリエステルフィルムの製
造方法に関するものである。
That is, in the present invention, after biaxial stretching of a polyester film, the tension in the film longitudinal direction is set to 10 Kg/m or less, and the temperature at the center of the film is set to 1zo0c or more and the temperature at the side edges is set to 100 C or higher using an infrared heater. The present invention relates to a method for producing a biaxially stretched polyester film, which is characterized by heating for 3 seconds or more so that the temperature is IO'C or more higher than the temperature at the center.

ポリエステルフィルムはポリエチレンテレフタレートフ
ィルムが代表的なものである。
A typical polyester film is polyethylene terephthalate film.

ポリエステルには無機顔料、有機顔料、抗酸化剤、紫外
線吸収剤等を適宜添加することができる。
Inorganic pigments, organic pigments, antioxidants, ultraviolet absorbers, etc. can be added to the polyester as appropriate.

二軸延伸は、縦、積別々に行なわれたものであってもよ
く、両方向同時に行なわれたものであってもよい。但し
、ベンディング現象は遂次二軸延伸特有のものである。
The biaxial stretching may be carried out separately in the longitudinal direction and in the longitudinal direction, or may be carried out simultaneously in both directions. However, the bending phenomenon is unique to sequential biaxial stretching.

二軸延伸終了後、ポリ二゛ステルフィルムは例えば第1
図に示すような装置で熱処理される。
After biaxial stretching, the polyester film is
Heat treatment is performed using the equipment shown in the figure.

この装置は加熱ゾーン11冷却ゾーンコ及びテンション
分離ゾーン3からなっている。加熱ゾーンlにはフィル
ム参を全幅にわたって加熱する長尺の赤外線ヒーター!
が設けられ、冷却ゾーンコには冷風を吹き出す冷風ダク
ト[が設けられている。二軸延伸が終了したフィルム弘
は第7図右下からこの熱処理装置に送、り込まれ、加熱
ゾーン11?lIゾーンコ及びテンション分離ゾーン3
を順次通過して巻き取られる。
This device consists of a heating zone 11, a cooling zone 1, and a tension separation zone 3. In the heating zone L, there is a long infrared heater that heats the entire width of the film!
The cooling zone is equipped with a cold air duct that blows out cold air. The film that has been biaxially stretched is fed into this heat treatment equipment from the bottom right of Fig. 7, and heated into the heating zone 11? lI zone co and tension separation zone 3
It is wound up after passing through it one after another.

本発明の方法においては、加熱手段として赤外線ヒータ
ーを用い、フィルムの幅方向に温度分布をもたせて加熱
するようにしたところに特徴がある。
The method of the present invention is characterized in that an infrared heater is used as the heating means, and the film is heated with a temperature distribution in the width direction.

赤外線ヒーターの種類は問うところではなく、セラミッ
クヒータ−、パイコールヒーター、シーズヒーターなど
を利用することができる。このヒーターはフィルムの幅
方向に温度分布をもたせるためにフィルムの長手方向と
平行に並べて配設する。その−例を第2図に示す。同図
に示すように、長尺の赤外線ユニットヒーターja、!
a、・・・、raがフィルム係上にその長尺方向と平行
に並べられている。ユニットヒーターjaの数はフィル
ム≠の@/m当り3〜10基程度、特に参〜を基程度が
適当である。赤外線ヒーターの全幅はフィルムの全幅を
所定の温度分布に加熱できるように定められ、通常はフ
ィルムの全幅と同じかそれよシやや広い程度である。一
方、赤外線ヒーターの全長はフィルムを所定時間所定温
度に加熱できればよく、これはヒーターの発熱能力、フ
ィルムの搬送速度などによって異なる。
The type of infrared heater does not matter, and ceramic heaters, Pycor heaters, sheathed heaters, etc. can be used. These heaters are arranged parallel to the longitudinal direction of the film in order to provide temperature distribution in the width direction of the film. An example is shown in FIG. As shown in the figure, a long infrared unit heater ja,!
a, . . . , ra are arranged on the film board parallel to its longitudinal direction. The number of unit heaters is suitably about 3 to 10 per m of film, particularly about 3 to 10 per m. The total width of the infrared heater is determined so that the entire width of the film can be heated to a predetermined temperature distribution, and is usually the same as or slightly wider than the total width of the film. On the other hand, the total length of the infrared heater only needs to be able to heat the film to a predetermined temperature for a predetermined time, and this varies depending on the heat generation capacity of the heater, the transport speed of the film, etc.

温度分布はフィルム中央部の温度が/J−℃C以上で側
縁部の温度が中央部の温度よシも1O0C以上高くなる
ようにする。中央部の温度は/J−0’c−−zoo 
0c程e、特に/60°C−、/1r℃C程度が一般に
適当であシ、側縁部の温度は140 ’CN220 ’
C程度、特に/1℃(:〜21℃(:程度が一般に適当
である。中央部と側縁部の温度差は10’C−6O’c
程度であり、通常はio’c−to’c程度が適当であ
る。加熱ゾーン出口におけるフィルム幅方向の温度分布
は通常舟底形になる。各ユニットヒーターはフィルムに
中たるみ、ベンディングなどを生じないように適宜コン
トロールされる。特に食中を分割スリットする際に、ベ
ンディングが問題となるが、その際、部分加熱を行ない
、各スリット品のベンディング修正を行なう事も可能で
ある。
The temperature distribution is such that the temperature at the center of the film is /J-°C or more and the temperature at the side edges is 100C or more higher than the temperature at the center. The temperature at the center is /J-0'c--zoo
A temperature of about 0c, especially /60°C-, /1r°C is generally appropriate, and the temperature at the side edge is 140'CN220'
The temperature difference between the center and the side edges is 10'C-6O'c.
Normally, about io'c-to'c is appropriate. The temperature distribution in the width direction of the film at the exit of the heating zone is generally boat-shaped. Each unit heater is appropriately controlled to prevent sagging or bending of the film. In particular, bending is a problem when dividing and slitting food products, but it is also possible to perform partial heating and correct the bending of each slit product.

熱処理によって縦方向に十分小さな熱収縮値になるよう
にするために加熱ゾーンにおけるフィルムの長手方向の
張力を/ OKg / m以下にする。この張力はフィ
ルムの平面性の確保なども考慮すると通常7〜/ OK
g / m程度が適当である。張力の調節は例えばフィ
ルムが掛架されるロールの一部あるいは全部を駆動ロー
ルとしてその駆動力を調節することによって行なうこと
ができる。
In order to achieve a sufficiently small thermal shrinkage value in the longitudinal direction by heat treatment, the tension in the longitudinal direction of the film in the heating zone is set to be less than /OKg/m. This tension is usually 7~/OK, taking into account ensuring the flatness of the film.
Approximately g/m is appropriate. The tension can be adjusted, for example, by using part or all of the rolls on which the film is hung as drive rolls and adjusting the driving force of the rolls.

加熱時間は3秒以上で必要な寸法安定性を確保しうるよ
うに定められ、これは加熱温度及びフィルムの搬送速度
などによって異なる。
The heating time is set to be 3 seconds or longer so as to ensure the necessary dimensional stability, and this varies depending on the heating temperature, film conveyance speed, etc.

加熱後は冷却ゾーンで徐冷して熱処理で発生した歪を解
消させる。この冷却はポリエステルのガラス転移温度ま
で3秒以上かけて十分に収縮させるのがよい。第7図の
装置の場合には、搬送されるフィルムμ上に設けられた
冷風ダク)7の略等間隔の吹出孔7から吹き出される冷
風によって徐冷されるようになっている。
After heating, it is slowly cooled in a cooling zone to eliminate distortion caused by heat treatment. This cooling is preferably carried out for 3 seconds or more to sufficiently shrink the polyester until it reaches the glass transition temperature. In the case of the apparatus shown in FIG. 7, the film μ is gradually cooled by cold air blown out from blowing holes 7 at approximately equal intervals in a cold air duct 7 provided on the film μ to be conveyed.

冷却されたフィルムは次にテンション分離を行ない、以
降適当な張力をかけ巻き取られるテンション分離は第1
図の様にサクションドラムゴムロール等の駆動ロールタ
をテンタール巻取間に設けることにより行なわれる。
The cooled film is then subjected to tension separation, after which an appropriate tension is applied and the film is wound up.
As shown in the figure, this is carried out by providing a driving roller such as a suction drum rubber roll between tenter windings.

(作用) ポリエステルフィルムは横延伸ゾーンで長手方向の収縮
応力がフィルム中央部に集中し、中央部が両側縁部より
遅れて延伸ゾーンから出てくる。
(Function) The shrinkage stress in the longitudinal direction of the polyester film is concentrated in the center of the film in the transverse stretching zone, and the center comes out of the stretching zone later than the edges on both sides.

その結果、第3図に示すようにフィルム≠に中たるみi
oを生じる。また、例えばフィルム≠を第μ図(1/!
にスリット)及び第5図(1/4にスリット)に示すよ
うにスリットすると中たるみlOに加えて側縁部の耳の
び//を生じるとともにフィルム参が長手方向に曲って
(ベンディング)出てくる。これらを前述の低張力下に
おける舟底形温度分布の加熱で除去している。
As a result, as shown in Figure 3, the film ≠ has a sag i
produces o. Also, for example, film ≠ is shown in μ (1/!
When the film is slit as shown in Fig. 5 (1/4 slit) and Fig. 5 (1/4 slit), in addition to the middle sag, the side edges are stretched out and the film is bent in the longitudinal direction (bending). come. These are removed by heating with a boat-bottom temperature distribution under the aforementioned low tension.

フィルム幅方向の寸法安定性はテンター後半の高温ゾー
ンで改良されるが、長手方向の寸法安定性はテンタ一時
にはフィルム両側縁部がクリップで保持されているため
、十分な寸法安定性が得られない。これもまた本発明の
熱処理の際に改良している。
The dimensional stability of the film in the width direction is improved in the high-temperature zone in the latter half of the tenter, but the dimensional stability in the longitudinal direction is not sufficiently stable because both edges of the film are held with clips when the tenter is in use. do not have. This is also improved during the heat treatment of the present invention.

(実施例) テンターを出たポリエチレンテレフタレートフィルムを
一旦巻き取シ、これを第1図及び第2図に示す装置で熱
処理した。加熱ゾーンlにおける張力を1oKq/mと
し、赤外線ヒーターjを調節して加熱ゾーンl出口にお
けるフィルム参の幅方向の温度分布が第を図に示すよう
な分布になるようにした。フィルム参の加熱ゾーン通過
時間は3秒になるようにした。冷却ゾーンコの通過時間
は3秒であり、定速ロールタのところのフィルム温度は
zo”cであった。
(Example) The polyethylene terephthalate film that came out of the tenter was once wound up and then heat-treated using the apparatus shown in FIGS. 1 and 2. The tension in the heating zone 1 was set to 1 Kq/m, and the infrared heater j was adjusted so that the temperature distribution in the width direction of the film at the exit of the heating zone 1 was as shown in the figure. The time taken for the film to pass through the heating zone was set to 3 seconds. The passage time through the cooling zone was 3 seconds, and the film temperature at the constant speed rotor was zo''c.

一方、比較のために各ユニットヒーター!aの発熱量を
均一にし、他は上記と同様にして熱処理を行なった。加
熱ゾーンl出口におけるフィルム≠の幅方向の温度分布
は第7図に示す通シであった。
Meanwhile, each unit heater for comparison! The heat treatment was performed in the same manner as above except that the calorific value of a was made uniform. The temperature distribution in the width direction of the film at the exit of the heating zone 1 was as shown in FIG.

その結果、舟底形の温度分布で加熱した場合には、全幅
フィルムは第ざ図に示すように、そしてAスリット品は
第11図に示すようになQ1平面性は著しく良化された
。一方、均一加熱した比較例においては、全部品が第2
図にそして員スリット品が第1−図に示すようになシ、
平面性は未処理品より著しく悪化した。未処理品は、全
部品が第io図にセしてAスリット品が第13図に示す
ような平面性のものであり、中たるみがかな9存在した
ほか耳のびもあった。
As a result, when heated with a boat-shaped temperature distribution, the Q1 flatness of the full-width film was significantly improved as shown in Figure 11, and the A-slit product was shown in Figure 11. On the other hand, in the comparative example where the heating was uniform, all the parts
As shown in Figure 1, the slit product is as shown in Figure 1.
The flatness was significantly worse than that of the untreated product. In the untreated product, all parts were set as shown in Fig. io, and the A-slit product was flat as shown in Fig. 13, and there was sag in the center and extension at the edges.

熱収縮性及びベンディングは下表に示す通りであった。Heat shrinkability and bending were as shown in the table below.

実施例品  未処理品 熱収率  MD=o、o3憾 MD=0 、 / 、4
幅ベンディング 左0.2露  左/、0露(V2スリ
ツ鵠) 右   O■    右λ、om* 3mのフ
ィルムの最大ベンテ ィング値 (発明の効果) ヒーターを長手方向に平行に分割したことによって、特
定の中たるみ、耳のび、ベンディングを修正し、平面性
の良好なフィルムを得ることができた。ベンディングの
解消により、原反から多軸取りする際にスリット間差を
無くすことができた。
Example product Untreated product heat yield MD=o, o3, MD=0, /, 4
Width bending Left 0.2 dew Left /, 0 dew (V2 slot) Right O■ Right λ, om* Maximum venting value for 3m film (effect of the invention) By dividing the heater parallel to the longitudinal direction, We were able to correct certain sagging, sagging, and bending, and obtain a film with good flatness. By eliminating bending, it was possible to eliminate the difference between slits when cutting multiple shafts from the original fabric.

熱処理によって寸法安定性のすぐれたフィルムを得るこ
とができた。クリップから解放された状態で熱処理を行
なっているところから特にMD方向の熱収縮が改良され
た。
A film with excellent dimensional stability could be obtained by heat treatment. Thermal shrinkage in the MD direction was particularly improved because the heat treatment was performed while released from the clips.

赤外線ヒーターの採用により、加熱時間を短縮し為加熱
ゾーンを短小化できた。ロール搬送方式の採用によって
エアー搬送方式よりも設備を簡略化できた。
By using an infrared heater, we were able to shorten the heating time and shorten the heating zone. By adopting the roll conveyance method, the equipment was simpler than the air conveyance method.

従来、加熱及び冷却に際し温度ムラを生じるためかえっ
て平面性を阻害するケースが多く、この温度ムラを解消
するため長大な冷却ゾーンを必要とした。しかし、フィ
ルム幅方向に温度分布を設けた本発明の方法にあっては
、この温度ムラによる平面性阻害が減少し、冷却ゾーン
を短小化できた。
In the past, in many cases, flatness was hindered because temperature unevenness occurred during heating and cooling, and a long cooling zone was required to eliminate this temperature unevenness. However, in the method of the present invention in which a temperature distribution is provided in the width direction of the film, the inhibition of flatness due to temperature unevenness is reduced, and the cooling zone can be shortened.

本発明の方法は省スペース下で実施できるので、製膜機
が既存していてスペースが限られている場合でも大規模
な改造を必要としない。
Since the method of the present invention can be carried out in a space-saving manner, it does not require large-scale modification even if the film forming machine already exists and space is limited.

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

第1図は本発明の方法の実施に利用される装置の一例の
概要を示す側面図であり、第2図はその加熱部分の部分
斜視図である。第3図〜第!図はテンターから出た状態
のフィルムの平面図であり、第3図は全部品、第参図は
員スリット品、そして第3図はV4スリット品をそれぞ
れ示している。 第を図は実施例において、そして第7図は比較例におい
て、いずれも加熱ゾーン出口のフィルムの幅方向温度分
布を示すものである。第を図〜第1O図はいずれも全部
品の平面図であシ、第r図は実施例品、第り図は比較例
品、そして第1Q図は未処理品をそれぞれ示している。 第1/図〜第73図はいずれもAスリット品の平面図で
ちゃ、第11図は実施例品、第1コ図は比較例品、そし
て第13図は未処理品をそれぞれ示している。
FIG. 1 is a side view showing an outline of an example of an apparatus used for carrying out the method of the present invention, and FIG. 2 is a partial perspective view of the heating portion thereof. Figure 3 ~ No. 3! The figure is a plan view of the film taken out from the tenter, FIG. 3 shows all parts, FIG. 3 shows a member slit product, and FIG. 3 shows a V4 slit product. Figure 7 shows the temperature distribution in the width direction of the film at the exit of the heating zone in the example and Figure 7 in the comparative example. Figures 1 to 1O are all plan views of all the parts. Figure R shows an example product, Figure 1 shows a comparative example product, and Figure 1Q shows an untreated product. Figures 1/73 are all plan views of the A-slit product, Figure 11 shows the example product, Figure 1 shows the comparative example product, and Figure 13 shows the untreated product. .

Claims (1)

【特許請求の範囲】[Claims] ポリエステルフィルムを、二軸延伸終了後、フィルム長
手方向の張力を10Kg/m以下とし、赤外線ヒーター
により該フィルム中央部の温度が150℃以上であつて
側縁部の温度が該中央部の温度よりも10℃以上高くな
るようにして加熱することを特徴とする二軸延伸ポリエ
ステルフィルムの製造方法
After the polyester film is biaxially stretched, the tension in the longitudinal direction of the film is set to 10 kg/m or less, and an infrared heater is used to raise the temperature of the center of the film to 150°C or higher and the temperature of the side edges to be lower than the temperature of the center. A method for producing a biaxially stretched polyester film, which comprises heating the film to a temperature of 10°C or more.
JP7353185A 1985-04-09 1985-04-09 Preparation of biaxially oriented polyester film Pending JPS61233523A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7353185A JPS61233523A (en) 1985-04-09 1985-04-09 Preparation of biaxially oriented polyester film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7353185A JPS61233523A (en) 1985-04-09 1985-04-09 Preparation of biaxially oriented polyester film

Publications (1)

Publication Number Publication Date
JPS61233523A true JPS61233523A (en) 1986-10-17

Family

ID=13520905

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7353185A Pending JPS61233523A (en) 1985-04-09 1985-04-09 Preparation of biaxially oriented polyester film

Country Status (1)

Country Link
JP (1) JPS61233523A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0299560A2 (en) * 1987-07-14 1989-01-18 Agfa-Gevaert N.V. Process for making a curled photographic film
US4892689A (en) * 1987-07-14 1990-01-09 Agfa-Gevaert N.V. Process for making curled photographic film
US5575968A (en) * 1994-05-06 1996-11-19 Skc Limited Process for the preparation of thermoplastic resin film
KR100369441B1 (en) * 1998-11-20 2003-03-17 에스케이씨 주식회사 Manufacturing method of biaxially oriented polyester film
WO2007086540A1 (en) * 2006-01-27 2007-08-02 Fujifilm Corporation Optical film and method for producing the same
JP2010076109A (en) * 2008-09-24 2010-04-08 Fujifilm Corp Film manufacturing method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5396072A (en) * 1977-02-02 1978-08-22 Teijin Ltd Preparation of polyester film with excellent dimensional stability
JPS59115812A (en) * 1982-12-23 1984-07-04 Teijin Ltd Method and device for manufacturing thermoplastic resin film

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5396072A (en) * 1977-02-02 1978-08-22 Teijin Ltd Preparation of polyester film with excellent dimensional stability
JPS59115812A (en) * 1982-12-23 1984-07-04 Teijin Ltd Method and device for manufacturing thermoplastic resin film

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0299560A2 (en) * 1987-07-14 1989-01-18 Agfa-Gevaert N.V. Process for making a curled photographic film
US4892689A (en) * 1987-07-14 1990-01-09 Agfa-Gevaert N.V. Process for making curled photographic film
US5575968A (en) * 1994-05-06 1996-11-19 Skc Limited Process for the preparation of thermoplastic resin film
KR100369441B1 (en) * 1998-11-20 2003-03-17 에스케이씨 주식회사 Manufacturing method of biaxially oriented polyester film
WO2007086540A1 (en) * 2006-01-27 2007-08-02 Fujifilm Corporation Optical film and method for producing the same
JP2010076109A (en) * 2008-09-24 2010-04-08 Fujifilm Corp Film manufacturing method

Similar Documents

Publication Publication Date Title
US4160799A (en) Maintaining planarity in polyester film during uniform temperature heat relaxation
KR960013068B1 (en) Thermoplastic resin film & a method for producing the same
JP2999379B2 (en) Relaxation heat treatment method for stretched film
JPS61233523A (en) Preparation of biaxially oriented polyester film
JPS6022616B2 (en) Method for manufacturing polyester film with excellent dimensional stability
JPS5824418A (en) Preparation of thermoplastic polyester film
JPH0617065B2 (en) Heat treatment method for biaxially stretched polyester film
JPS62183328A (en) Manufacture of biaxially oriented film and device used for this method
KR101709968B1 (en) Low shrinkage film producting apparatus and method of manufacturing the same
JP3830107B2 (en) Method for improving flatness of thermoplastic film
JPS62268629A (en) Heat treating method for thermoplastic resin film
JPH06166102A (en) Manufacture of polyester film
JPH04292937A (en) Manufacture of thermoplastic resin film
JPS6021053B2 (en) Cooling method for biaxially oriented polyester film
JPH0586905B2 (en)
JPH0457182B2 (en)
JPH0358584B2 (en)
JPH0245976B2 (en) NIJIKUENSHINHORIIIPUSHIRONNKAPUROAMIDOFUIRUMUNOSEIZOHOHO
JP2002192609A (en) Manufacturing method of biaxially oriented polyester film
JPS62183327A (en) Manufacture of biaxially oriented film
JP2525501B2 (en) Method for producing polyester film
JPH04292934A (en) Manufacture of thermoplastic resin film
JP2002001810A (en) Method for relaxation heat treating biaxially oriented polyester film
JPH03106635A (en) Method of heat-treating crystalline thermoplastic resin film and apparatus therefor
US7200904B2 (en) Tenter system