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JPS62183328A - Manufacture of biaxially oriented film and device used for this method - Google Patents

Manufacture of biaxially oriented film and device used for this method

Info

Publication number
JPS62183328A
JPS62183328A JP61024154A JP2415486A JPS62183328A JP S62183328 A JPS62183328 A JP S62183328A JP 61024154 A JP61024154 A JP 61024154A JP 2415486 A JP2415486 A JP 2415486A JP S62183328 A JPS62183328 A JP S62183328A
Authority
JP
Japan
Prior art keywords
film
zone
temperature
tenter
biaxially oriented
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
JP61024154A
Other languages
Japanese (ja)
Other versions
JPH0455377B2 (en
Inventor
Hideo Kato
秀雄 加藤
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 JP61024154A priority Critical patent/JPS62183328A/en
Publication of JPS62183328A publication Critical patent/JPS62183328A/en
Publication of JPH0455377B2 publication Critical patent/JPH0455377B2/ja
Granted legal-status Critical Current

Links

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  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To obtain a biaxially oriented film whose part having balanced physical properties and high uniformity has been widened, by a method wherein a preheating zone is provided between a lateral orienting zone and a heat treatment zone and a heating temperature is controlled from a high temperature to a low temperature toward the central part from an end part under a state where both end sides of the film is held by a tenter. CONSTITUTION:Although a thermoplastic film uniaxially oriented in a longitudinal direction is oriented laterally by a tenter and made into a biaxially oriented film by applying heat treatment to the same, a temperature gradient varying from high temperature to low temperature from an end part to the center part of the film is applied to the film in a preheating zone and preheat treatment is applied to the same while keeping a film temperature of the center part at less than 90 deg.C after providing the preheating zone between a lateral orienting zone and a heat treatment zone in the tenter. Then the film temperature posterior to the lateral orientation is lowered, which becomes profitable for post treatment, by providing a neutral zone between the lateral orienting zone and preheating zone in the tenter. A part corresponding to the upper bottom of a trapezoid shows uniform physical properties in a widthward direction by applying preheat treatment to the film posterior to the lateral orientation.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は二軸配向フィルムの製造方法及びこれに用いる
装置に関し、更に詳しくは縦方向に一軸延伸をした熱可
塑性フィルムをテンターにより横延伸熱処理する際に生
じるボーイングを抑え、二輪方向の物性がバランスした
均一性の高いフィルムを幅広く有効に製造する方法及び
このフィルムの製造に用いる装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for producing a biaxially oriented film and an apparatus used therein, and more specifically, to a method for producing a biaxially oriented film, and more specifically to a process in which a thermoplastic film uniaxially stretched in the longitudinal direction is subjected to transverse stretching heat treatment using a tenter. The present invention relates to a method for widely and effectively manufacturing a highly uniform film with balanced physical properties in the direction of two wheels, and an apparatus used for manufacturing this film.

従来技術 二軸配向フィルム特に二軸配向ポリエステルフィルムは
工業的に広く用いられているが、特に写真、製図、磁気
ディスク等の用途では縦横両方向の物性、とりわけ温度
膨張率、湿度膨張率がバランスしていることが望まれる
。また製品フィルムのどの部分においても同じ性質であ
ることが望ましい。
BACKGROUND ART Biaxially oriented films, especially biaxially oriented polyester films, are widely used industrially, but in particular for applications such as photography, drafting, and magnetic disks, physical properties in both the vertical and horizontal directions, especially the thermal expansion coefficient and the humidity expansion coefficient, are not well balanced. It is desirable that the It is also desirable that the properties be the same in all parts of the product film.

しかし、通常の逐次二輪延伸方法、すなわち縦延伸につ
づいて横延伸を施す方法において製品フィルムの幅方向
(横方向)の物性を均一にすることは極めて困難であっ
た。この理由は、テンター内においてフィルムの両側端
は把持されていて、横延伸に伴う縦方向のフィルム収縮
応力が把持手段であるクリップ等によって強く拘束され
るのに対し、フィルム中央部分は把持手段による拘束力
の影響が弱くなり、このため上記収縮応力によってフィ
ルムの中央部分の進展が遅れることにある。
However, it has been extremely difficult to make the physical properties of the product film uniform in the width direction (transverse direction) using the usual sequential two-wheel stretching method, that is, a method in which longitudinal stretching is followed by lateral stretching. The reason for this is that both ends of the film are gripped in the tenter, and the shrinkage stress of the film in the longitudinal direction due to horizontal stretching is strongly restrained by the gripping means such as clips. The effect of the restraining force is weakened, and therefore the expansion of the central portion of the film is delayed due to the shrinkage stress.

仮に、横延伸前にフィルム面上に横方向に沿って直線を
描いておくと、横延伸に伴ってこの直線は変形しフィル
ム進行方向に向って凹形に曲るようになる。この現象は
ボーイングと称されるものであるが、このボーイング現
象がフィルム横方向の物性、特に温度膨張率、湿度膨張
率を不均一にする原因となっている。この現象によって
、フィルムの両端部分ではボーイング線に対して更に縦
方向に傾斜した配向主軸が生じ、この主軸方向の温度膨
張率、湿度膨張率は一層低くなり、主軸方向に対して直
角な方向での両値は高くなる傾向がある。
If a straight line is drawn along the lateral direction on the film surface before lateral stretching, this straight line will be deformed and curved into a concave shape in the direction of film travel as the film is stretched. This phenomenon is called bowing, and this bowing phenomenon causes non-uniformity in the physical properties of the film in the lateral direction, particularly the temperature expansion coefficient and the humidity expansion coefficient. As a result of this phenomenon, a principal axis of orientation is created at both ends of the film that is further inclined vertically with respect to the bowing line, and the coefficient of temperature expansion and coefficient of humidity expansion in the direction of this principal axis becomes lower, and in the direction perpendicular to the principal axis. Both values tend to be high.

このような両輪方向の物性の差異を減少ないし解消する
方法として、特開昭50−73978号公報には横延伸
工程と熱処理工程との間に、ニップロールを置くフィル
ムの製法が提案されている。
As a method for reducing or eliminating such a difference in physical properties in both wheel directions, Japanese Patent Application Laid-Open No. 50-73978 proposes a film manufacturing method in which a nip roll is placed between the transverse stretching process and the heat treatment process.

しかし、この技術はフィルム表面にニップロールによる
傷が発生する慣れがあり、実用面で著しく制約される。
However, this technique has a habit of causing scratches on the film surface due to nip rolls, which severely limits its practical use.

また特開昭51−80372号公報、特開昭54−13
7076号公報にはボーイング減少対策を開示している
ものの、この延伸は同時二輪延伸によるものである。こ
のように逐次二輪延伸においてボーイング現象を回避(
減少)せしめて、物性の均一化をもたらす延伸方法は未
だ開発されていない。
Also, JP-A-51-80372, JP-A-54-13
Although the publication No. 7076 discloses measures to reduce bowing, this stretching is based on simultaneous two-wheel stretching. In this way, the bowing phenomenon is avoided in sequential two-wheel stretching (
At the very least, a stretching method that brings about uniformity of physical properties has not yet been developed.

発明の目的 本発明の目的はフィルム端部のボーイングを強制的に大
きくしかつフィルム中央部のボーイング差を著しく小さ
くして、物性のバランスした均一性の高い部分を幅広く
した二軸配向フィルムの製造方法及びこれに用いる装置
を提供することにある。
Purpose of the Invention The purpose of the present invention is to produce a biaxially oriented film in which the bowing at the edges of the film is forcibly increased and the difference in bowing at the center of the film is significantly reduced, thereby widening the area with balanced physical properties and high uniformity. An object of the present invention is to provide a method and a device used therefor.

発明の構成・効果 本発明の目的は、本発明によれば、 縦方向に一軸延伸をした熱可塑性フィルムをテンターに
より横方向に延伸し、ついで熱処理を施す二軸配向フィ
ルムの製造方法において、横延伸ゾーンと熱処理ゾーン
の間に予熱ゾーンを設け、該予熱ゾーンにてフィルムの
端部より中央部に向って高温から低温への温度勾配をつ
け、かつ中央部のフィルム温度を90℃以下に保って予
熱処理を施すことを特徴とする二軸配向フィルムの製造
方法、並びに 縦方向に一軸延伸をした熱可塑性フィルムの両側端を把
持して横方向に延伸し、ついで熱処理を施すテンターに
おいて、横延伸ゾーンと熱処理ゾーンの間に、フィルム
両側端を把持した状態で、該端部より中央部に向って高
温から低温に加熱温度を調節できる加熱手段を備えた予
熱ゾーンを設けたことを特徴とする二軸配向フィルム製
造用テンター によって達成される。
Structure and Effects of the Invention According to the present invention, the present invention provides a method for producing a biaxially oriented film in which a thermoplastic film that has been uniaxially stretched in the longitudinal direction is stretched in the transverse direction using a tenter, and then subjected to heat treatment. A preheating zone is provided between the stretching zone and the heat treatment zone, and in the preheating zone, a temperature gradient is created from a high temperature to a low temperature from the edge of the film toward the center, and the film temperature in the center is maintained at 90°C or less. A method for producing a biaxially oriented film, which is characterized in that a thermoplastic film that has been uniaxially stretched in the longitudinal direction is gripped at both ends, stretched in the transverse direction, and then subjected to a heat treatment. A preheating zone is provided between the stretching zone and the heat treatment zone, and is equipped with a heating means that can adjust the heating temperature from a high temperature to a low temperature from the ends toward the center while holding both ends of the film. This is achieved by a tenter for producing biaxially oriented films.

本発明において熱可塑性ポリマーとは、二軸配向フィル
ムとなし得るものであれば何ら限定されない0例えば、
ポリエチレンテレフタレート、ポリエチレン−2,6−
ナフタレンジカルボキシレート、ポリ−1,4−シクロ
ヘキシレンジメチレンテレフタレート、ポリテトラメチ
レンテレフタレートなどの如きポリエステル;ナイロン
6、ナイロン6.6などの如きポリアミド;ポリプロピ
レンの如きポリオレフィン:ポリフェニレンサルファイ
ド等の合成ポリマーが挙げられる。これらは単体であっ
ても混合物、共重合物であってもよい。好適なポリマー
としてはポリエステル特にポリエチレンテレフタレート
が挙げられる。またこれらは少量の無機添加物や有機添
加物を含んでいてもよい。
In the present invention, the thermoplastic polymer is not limited in any way as long as it can be made into a biaxially oriented film.For example,
Polyethylene terephthalate, polyethylene-2,6-
Polyesters such as naphthalene dicarboxylate, poly-1,4-cyclohexylene dimethylene terephthalate, polytetramethylene terephthalate, etc.; polyamides such as nylon 6, nylon 6.6, etc.; polyolefins such as polypropylene; synthetic polymers such as polyphenylene sulfide. Can be mentioned. These may be used alone, as a mixture, or as a copolymer. Suitable polymers include polyesters, especially polyethylene terephthalate. They may also contain small amounts of inorganic or organic additives.

かかる熱可塑性ポリマーを用いて二軸配向フィルムを製
造する方法は、従来から蓄積された公知の方法で未延伸
フィルムを得、これを縦横逐次二軸延伸する方法による
ことができ、特に熱可塑性ポリマーをグイ(例えばTダ
イ)から溶融押出し、冷却回転ドラム上で急冷し、次い
で延伸配向温度で縦方向に延伸し続いてテンターにて横
方向に延伸し、熱処理する方法によることが好ましい。
A method for producing a biaxially oriented film using such a thermoplastic polymer can be a method of obtaining an unstretched film by a conventionally known method and sequentially biaxially stretching it in the longitudinal and lateral directions. It is preferable to use a method in which the material is melt-extruded from a gooey (for example, a T-die), rapidly cooled on a cooling rotating drum, then stretched in the longitudinal direction at a stretching orientation temperature, then stretched in the transverse direction in a tenter, and heat treated.

縦方向の延伸は2つのロール間の速度差(供給ロールと
延伸ロールの速度差)を利用してのロール延伸法による
のが好ましい。その際、縦方向の延伸は1段延伸でも良
く、また多段延伸でも良い。
The stretching in the longitudinal direction is preferably carried out by a roll stretching method that utilizes the speed difference between two rolls (the speed difference between the supply roll and the stretching roll). At this time, the stretching in the longitudinal direction may be performed in one stage or in multiple stages.

本発明においては縦方向に一軸延伸をした熱可塑性フィ
ルムをテンターにより横方向に延伸し、ついで熱処理を
施して二軸配向フィルムとするが、テンターにおいて横
延伸ゾーンと熱処理ゾーンとの間に予熱ゾーンを設け、
該予熱ゾーンにてフィルムの端部より中央部に向って高
温から低温への温度勾配をつけ、かつ中央部のフィルム
温度を90℃以下に保って予熱処理を施す。予熱ゾーン
の長さは、フィルムの走行スピードまた厚さによって異
なるが、フィルムの滞留時間を3秒以上とりうる長さで
あることが好ましい。また、幅方向の温度勾配をつける
方法は、フィルムの幅方向に細かく区分した各スリット
より所定温度の熱風を吹きつける方法、複数個の赤外線
ヒーターをフィルムの進行方向に平行に並べ各ヒータ一
温度を調節する方法あるいは前記ヒーターの設置間隔を
端部から中央部に向って、密から粗にする方法、あるい
はそれらの組み合せ等が例示できるが、これらの方法に
限るものではない。この予熱処理工程でのフィルム温度
は端部から中央部に向って高温から低温へと温度勾配を
つけるが、該温度勾配は連続的でも段階的でもよい。し
かし、フィルムの中央部の温度は90℃以下とする。こ
れは中央部の温度が高温になる程フィルムの厚み斑が悪
くなる為であり、この温度が90℃より高くなると極端
にフィルムの厚み斑が劣るようになる。この中央部のフ
ィルム温度はガラス転移温度以下に保つと厚み斑が良好
となり、最も好ましい。フィルム端部からの温度勾配と
は、フィルム把持具の近傍からという意味であり、クリ
ップ等の把持部分での切断対策等の為に把持部の直近の
温度を低温に保つことは許されるものである。加熱温度
は処理時間やフィルムの配向度に依存するもので一概に
はきめられないが、端部の高温部は少なくとも中央部の
温度より10℃以上高温であるのが好ましい。また該温
度は引きつづき行う熱処理温度より低いのが好ましい。
In the present invention, a thermoplastic film that has been uniaxially stretched in the longitudinal direction is stretched in the transverse direction using a tenter, and then heat-treated to obtain a biaxially oriented film. established,
Preheating treatment is performed in the preheating zone by creating a temperature gradient from high temperature to low temperature from the edges of the film toward the center, and maintaining the film temperature at the center below 90°C. The length of the preheating zone varies depending on the running speed and thickness of the film, but it is preferably long enough to allow the film to stay for 3 seconds or more. In addition, methods for creating a temperature gradient in the width direction include blowing hot air at a predetermined temperature through each slit that is finely divided in the width direction of the film, and arranging multiple infrared heaters in parallel to the direction of film travel, each heater having one temperature. Examples include a method of adjusting the spacing of the heaters, a method of increasing the installation interval of the heaters from close to coarse from the ends toward the center, or a combination thereof, but the method is not limited to these methods. The temperature of the film in this preheating step has a temperature gradient from high temperature to low temperature from the ends to the center, and the temperature gradient may be continuous or stepwise. However, the temperature at the center of the film is 90° C. or lower. This is because the higher the temperature at the center, the worse the thickness unevenness of the film becomes, and when this temperature rises above 90°C, the thickness unevenness of the film becomes extremely poor. It is most preferable to keep the film temperature at the center below the glass transition temperature, since thickness unevenness will be improved. The temperature gradient from the edge of the film means from the vicinity of the film gripping tool, and it is not permissible to keep the temperature in the immediate vicinity of the gripping part low in order to prevent cutting at the gripping part such as a clip. be. The heating temperature depends on the processing time and the degree of orientation of the film and cannot be determined unconditionally, but it is preferable that the high temperature portions at the ends are at least 10° C. higher than the temperature in the center. Further, the temperature is preferably lower than the temperature of the subsequent heat treatment.

熱処理温度より低い場合はその後の熱処理により幅方向
の結晶化度を均一に出来るが、高い場合には該処理部の
み結晶化度が高くなり、幅方向に物性差が生じフィルム
の幅歩留が低下する。
If it is lower than the heat treatment temperature, the crystallinity degree in the width direction can be made uniform by the subsequent heat treatment, but if it is higher, the crystallinity degree will be high only in the treated area, resulting in differences in physical properties in the width direction, and the width yield of the film will be reduced. descend.

横延伸後のフィルムに上述の予熱処理を施すことにより
、フィルム端部に大きな収縮力が生じ、該端部がフィル
ムの進行方向に対し大幅に遅れ、同時にフィルム中央部
に向って収縮力は徐々に小さくなり、これに伴って進行
方向に対する遅れも徐々に小さくなるので、ボーイング
の形は第1図に示す如き弓形から第2図に示す如きほぼ
台形に修正される。台形の上底部に当る部分は幅方向に
均一な物性となっている。
By subjecting the film after horizontal stretching to the above-mentioned preheating treatment, a large shrinkage force is generated at the edges of the film, and the edges are significantly delayed with respect to the film's traveling direction, and at the same time, the shrinkage force gradually decreases toward the center of the film. As the delay in the direction of movement gradually decreases, the shape of the bowing is modified from an arc as shown in FIG. 1 to a nearly trapezoid as shown in FIG. The part corresponding to the upper base of the trapezoid has uniform physical properties in the width direction.

本発明においてテンターの横延伸ゾーン及び熱処理ゾー
ンは従来から公知のもので良く、またその条件も従来か
ら蓄積されたものを採用することができる。またテンタ
ーには横延伸ゾーンと予熱ゾーンとの間にニュートラル
ゾーンを設けることができる。このニュートラルゾーン
を設けることで横延伸後のフィルム温度が低下し、その
後の処理に有利となる。
In the present invention, the transverse stretching zone and the heat treatment zone of the tenter may be conventionally known ones, and the conditions can also be those that have been accumulated in the past. Moreover, a neutral zone can be provided in the tenter between the transverse stretching zone and the preheating zone. By providing this neutral zone, the temperature of the film after lateral stretching is lowered, which is advantageous for subsequent processing.

上記熱処理においては所定の温度・・・・・・例えばポ
リエチレンテレフタレートフィルムの場合200〜23
0℃・・・・・・でフィルム全体を定幅加熱するとよい
In the above heat treatment, a predetermined temperature...for example, 200 to 23
It is preferable to heat the entire film at a constant temperature of 0°C.

本発明によれば、フィルム幅方向に沿って物性の均一な
二軸配向熱可塑性フィルムが高い歩留りで得られる。そ
して該フィルムを用いて例えばフレキシブル磁気ディス
クを製造すると、温度膨張率、湿度膨張率のバランスし
た高賞品のディスクを高い歩留りで製造することができ
る。
According to the present invention, a biaxially oriented thermoplastic film having uniform physical properties along the film width direction can be obtained at a high yield. When the film is used to manufacture, for example, a flexible magnetic disk, a highly prized disk with a well-balanced thermal expansion coefficient and humidity expansion coefficient can be manufactured at a high yield.

実施例 以下、実施例を掲げて本発明を更に説明する。Example The present invention will be further explained below with reference to Examples.

実施例1 ポリエチレンテレフタレートを溶融してTダイより押出
し、冷却回転ドラム表面でフィルム状に成形して冷却し
たのち、縦方向に80℃で3.6倍延伸しミ続いて横延
伸ゾーン、ニュートラルゾーン、予熱ゾーン及び熱固定
ゾーンを備えたテンターにて延伸熱処理を行った。上記
横延伸ゾーンでは、フィルムを熱風加熱で90℃に上昇
して3.9倍に走行速度10m/a+inで延伸した。
Example 1 Polyethylene terephthalate was melted and extruded through a T-die, formed into a film on the surface of a cooling rotating drum, cooled, and then stretched 3.6 times in the longitudinal direction at 80°C, followed by a transverse stretching zone and a neutral zone. The stretching heat treatment was performed in a tenter equipped with a preheating zone and a heat fixing zone. In the transverse stretching zone, the film was heated to 90° C. by hot air heating and stretched 3.9 times at a running speed of 10 m/a+in.

上記予熱ゾーンは長さ1mで、直径10mφ長さ90c
11の赤外線ヒーターを両端部よりそれぞれ401Fl
ピツチで12本取りつけてあり、各ヒーターの温度調節
によってフィルム両端部の温度が110℃となるように
、かつこれより中央部に向って温度を徐々に下げて端部
よりそれぞれ50C11の位置の温度が70℃になるよ
うに加熱し、更に中央部のフィルム温度は60℃に保っ
た。
The above preheating zone has a length of 1m and a diameter of 10mφ and a length of 90cm.
11 infrared heaters each 401F from both ends
Twelve heaters are installed in a pitch, and by adjusting the temperature of each heater, the temperature at both ends of the film is 110℃, and the temperature is gradually lowered from this point toward the center, and the temperature at a position 50C11 from each edge is adjusted. was heated to 70°C, and the film temperature at the center was maintained at 60°C.

上記熱固定ゾーンには、180℃に保った長さ1.5m
の熱風加熱ゾーンと、これに続り190℃に保った長さ
3mの熱風加熱ゾーンとを設けた。テンターより出た二
軸配向フィルムは常法により常温に冷却し、ロールに捲
き取った。このフィルムのボーイングの形は第2図に似
たものでほぼ台形であった。
The above heat fixation zone has a length of 1.5m kept at 180℃.
A hot air heating zone with a length of 3 m maintained at 190° C. was provided. The biaxially oriented film that came out of the tenter was cooled to room temperature by a conventional method and wound up onto a roll. The shape of the Boeing in this film was similar to that shown in Figure 2, and was almost trapezoidal.

実施例2 予熱ゾーンにおけるフィルム両端部の温度を120℃、
端部より50ヨmの位置の温度をそれぞれ85℃、更に
フィルム中央部の温度を85℃とする以外は実施例1と
同様に行って二軸配向フィルムを得た。
Example 2 The temperature at both ends of the film in the preheating zone was set to 120°C.
A biaxially oriented film was obtained in the same manner as in Example 1, except that the temperature at the position 50 m from the end was 85°C, and the temperature at the center of the film was 85°C.

このフィルムのボーイングの形は実施例1のときと同じ
ように第2図に近いものであった。
The bowing shape of this film was similar to that shown in FIG. 2 as in Example 1.

比較例1 予熱ゾーンにおいて赤外線ヒーターに通電せず、該ヒー
ターによる加熱を行わない以外は実施例1と同様に実施
して二軸配向フィルムを得た。このフィルムのボーイン
グは第1図に似た弓形であった。
Comparative Example 1 A biaxially oriented film was obtained in the same manner as in Example 1, except that the infrared heater was not energized in the preheating zone and no heating was performed by the heater. The bowing in this film was arcuate, similar to Figure 1.

これらのフィルムのボーイング量(弦と孤の最大距M)
が3011以内で且つフィルムの温度膨張率の円周方向
の最大値と最小値の差が0.20 X 10−’/℃以
内となるフィルムのを効幅は、実施例1では170aa
、実施例2では150cmと幅広く、一方比較例1では
60cmにすぎなかった。また、フィルムの幅方向の厚
み斑は実施例1では4%、実施例2では7%、比較例1
では4%であった。
Bowing amount of these films (maximum distance between string and arc M)
is within 3011 and the difference between the maximum value and the minimum value of the temperature expansion coefficient of the film in the circumferential direction is within 0.20 x 10-'/°C. In Example 1, the effective width is 170 aa.
In Example 2, the width was as wide as 150 cm, while in Comparative Example 1, it was only 60 cm. In addition, the thickness unevenness in the width direction of the film was 4% in Example 1, 7% in Example 2, and Comparative Example 1.
It was 4%.

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

第1図、第2図は延伸フィルムのボーイングの形状を示
す図である。 力 11ヨ 尤21a
FIGS. 1 and 2 are diagrams showing the bowing shape of the stretched film. Power 11yo 21a

Claims (1)

【特許請求の範囲】 1、縦方向に一軸延伸をした熱可塑性フィルムをテンタ
ーにより横方向に延伸し、ついで熱処理を施す二軸配向
フィルムの製造方法において、横延伸ゾーンと熱処理ゾ
ーンの間に予熱ゾーンを設け、該予熱ゾーンにてフィル
ムの端部より中央部に向って高温から低温への温度勾配
をつけ、かつ中央部のフィルム温度を90℃以下に保っ
て予熱処理を施すことを特徴とする二軸配向フィルムの
製造方法。 2、予熱ゾーンにて中央部のフィルム温度をポリマーの
ガラス転移温度以下に保って予熱処理を施す特許請求の
範囲第1項記載の二軸配向フィルムの製造方法。 3、縦方向に一軸延伸をした熱可塑性フィルムの両側端
を把持して横方向に延伸し、ついで熱処理を施すテンタ
ーにおいて、横延伸ゾーンと熱処理ゾーンの間に、フィ
ルム両側端を把持した状態で、該端部より中央部に向っ
て高温から低温に加熱温度を調節できる加熱手段を備え
た予熱ゾーンを設けたことを特徴とする二軸配向フィル
ム製造用テンター。
[Claims] 1. In a method for producing a biaxially oriented film in which a thermoplastic film that has been uniaxially stretched in the longitudinal direction is stretched in the transverse direction using a tenter and then heat treated, preheating is performed between the transverse stretching zone and the heat treatment zone. The film is characterized by providing a zone, creating a temperature gradient from high temperature to low temperature from the edge of the film toward the center in the preheating zone, and performing preheating treatment while maintaining the film temperature in the center at 90°C or less. A method for producing a biaxially oriented film. 2. The method for producing a biaxially oriented film according to claim 1, wherein the preheating treatment is carried out in the preheating zone by maintaining the film temperature at the center below the glass transition temperature of the polymer. 3. In a tenter that grips both ends of a thermoplastic film that has been uniaxially stretched in the vertical direction, stretches it in the horizontal direction, and then heat-treats it, the film is held between the horizontal stretching zone and the heat treatment zone while gripping both ends of the film. A tenter for producing a biaxially oriented film, characterized in that a preheating zone is provided with a heating means that can adjust the heating temperature from a high temperature to a low temperature from the end toward the center.
JP61024154A 1986-02-07 1986-02-07 Manufacture of biaxially oriented film and device used for this method Granted JPS62183328A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61024154A JPS62183328A (en) 1986-02-07 1986-02-07 Manufacture of biaxially oriented film and device used for this method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61024154A JPS62183328A (en) 1986-02-07 1986-02-07 Manufacture of biaxially oriented film and device used for this method

Publications (2)

Publication Number Publication Date
JPS62183328A true JPS62183328A (en) 1987-08-11
JPH0455377B2 JPH0455377B2 (en) 1992-09-03

Family

ID=12130423

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61024154A Granted JPS62183328A (en) 1986-02-07 1986-02-07 Manufacture of biaxially oriented film and device used for this method

Country Status (1)

Country Link
JP (1) JPS62183328A (en)

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US5676902A (en) * 1994-07-04 1997-10-14 Skc Limited Process for the preparation of thermoplastic resin film
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JPH07285173A (en) * 1994-04-20 1995-10-31 Toray Ind Inc Electric insulating biaxially oriented polyethylene naphthalate film
US5575968A (en) * 1994-05-06 1996-11-19 Skc Limited Process for the preparation of thermoplastic resin film
US5676902A (en) * 1994-07-04 1997-10-14 Skc Limited Process for the preparation of thermoplastic resin film
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US7740919B2 (en) 2001-05-30 2010-06-22 Konica Corporation Cellulose ester film, its manufacturing method, optical retardation film, optical compensation sheet, elliptic polarizing plate, and image display
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JPWO2016152885A1 (en) * 2015-03-25 2018-01-25 東洋紡株式会社 Heat-shrinkable polyester film and package
US9944012B2 (en) 2015-03-25 2018-04-17 Toyobo Co., Ltd. Heat-shrinkable polyester film and package

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