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JPH0771822B2 - Method for producing polyester film - Google Patents
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JPH0771822B2 - Method for producing polyester film - Google Patents

Method for producing polyester film

Info

Publication number
JPH0771822B2
JPH0771822B2 JP33055988A JP33055988A JPH0771822B2 JP H0771822 B2 JPH0771822 B2 JP H0771822B2 JP 33055988 A JP33055988 A JP 33055988A JP 33055988 A JP33055988 A JP 33055988A JP H0771822 B2 JPH0771822 B2 JP H0771822B2
Authority
JP
Japan
Prior art keywords
film
stretching
birefringence
stretched
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 - Fee Related
Application number
JP33055988A
Other languages
Japanese (ja)
Other versions
JPH02175130A (en
Inventor
滋夫 内海
吉之丞 富高
裕二郎 福田
崇利 三木
Original Assignee
ダイアホイルヘキスト株式会社
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 ダイアホイルヘキスト株式会社 filed Critical ダイアホイルヘキスト株式会社
Priority to JP33055988A priority Critical patent/JPH0771822B2/en
Publication of JPH02175130A publication Critical patent/JPH02175130A/en
Publication of JPH0771822B2 publication Critical patent/JPH0771822B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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】 〔産業上の利用分野〕 本発明は厚み均一性および寸法安定性に優れた配向ポリ
エステルフィルムの製造方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing an oriented polyester film having excellent thickness uniformity and dimensional stability.

〔従来の技術および発明が解決しようとする課題〕[Problems to be Solved by Conventional Techniques and Inventions]

配向ポリエステルフィルムは、非晶状態のポリエステル
フィルムを縦及び/又は横方向に延伸して製造される。
そしてその製造条件、特に縦延伸条件を適宜選択するこ
とにより、フィルムの機械的諸特性は、ある程度まで、
そのフィルムの使用目的に適した範囲内とすることがで
きる。
The oriented polyester film is produced by stretching a polyester film in an amorphous state in the machine direction and / or the transverse direction.
And by appropriately selecting the production conditions, especially the longitudinal stretching conditions, the mechanical properties of the film are, to some extent,
It may be within the range suitable for the intended use of the film.

しかしながら、ある特定の特性を満足させようとすると
他の特性及び/又は生産性を多少犠牲にしなければなら
ず、全ての特性を満たすフィルムの製造は困難であっ
た。特にフィルムの厚み均一性および寸法安定性はフィ
ルムに要求される基本的な特性であり、これらの特性を
フィルムに付与するため、種々の試みがなされている
が、余分な解決に至っていない。
However, in order to satisfy one specific property, other properties and / or productivity have to be sacrificed to some extent, and it has been difficult to manufacture a film satisfying all the properties. In particular, the film thickness uniformity and dimensional stability are the basic properties required of the film, and various attempts have been made to impart these properties to the film, but no extra solution has been reached.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明者らは上記課題に鑑み、鋭意検討した結果、縦延
伸工程をある特定の条件で実施することにより、各種の
特性に優れたフィルムを容易に製造できることを見出
し、本発明を完成するに至った。
In view of the above problems, the present inventors have conducted intensive studies, and as a result of carrying out the longitudinal stretching step under certain specific conditions, they found that a film excellent in various characteristics can be easily produced, and to complete the present invention. I arrived.

すなわち本発明の要旨は、ポリエチレンテレフタレート
を主成分とする、実質的に非晶状態のフィルムを、縦方
向に総合延伸倍率4.0〜9.0倍で延伸した後、横方向に3.
2倍以上で延伸して配向フィルムを製造する方法におい
て、該縦方向の延伸が、 (A)非晶状態のフィルムを延伸倍率1.2〜4.0倍で複屈
折率が1×10-3〜2.5×10-2となるように1段または多
段で縦延伸し、 (B)フィルム温度をガラス転移点以下に冷却すること
なく、延伸倍率1.1〜3.5倍で複屈折率が3.5×10-2〜8.0
×10-2となるように1段または多段で縦延伸し、 (C)フィルム温度を前記(B)工程のフィルム温度未
満かつ(95-250・Δn)〜(130-250・Δn)℃の範囲
(但しΔnは縦方向の延伸後、横方向の延伸前における
フィルムの複屈折率を示す)とし、1段または多段で縦
延伸する工程 からなることを特徴とするポリエステルフィルムの製造
方法に存する。
That is, the gist of the present invention is that a film containing polyethylene terephthalate as a main component and in a substantially amorphous state is stretched in the longitudinal direction at a total stretching ratio of 4.0 to 9.0 times, and then in the transverse direction.
In the method for producing an oriented film by stretching at a draw ratio of 2 times or more, the stretching in the machine direction is (A) a film in an amorphous state having a draw ratio of 1.2 to 4.0 and a birefringence of 1 × 10 −3 to 2.5 ×. The film is longitudinally stretched in one step or in multiple steps so that it becomes 10 -2, and (B) the birefringence is 3.5 × 10 -2 to 8.0 at a draw ratio of 1.1 to 3.5 without cooling the film temperature below the glass transition point.
The film is longitudinally stretched in one step or in multiple steps so as to be × 10 -2, and (C) the film temperature is lower than the film temperature in the step (B) and (95-250 · Δn) to (130-250 · Δn) ° C. In the method for producing a polyester film, the range (where Δn is the birefringence index of the film after stretching in the longitudinal direction and before stretching in the transverse direction) is defined by a step of longitudinal stretching in one step or in multiple steps. .

以下、本発明を詳細に説明する。Hereinafter, the present invention will be described in detail.

本発明において使用されるポリエチレンテレフタレート
(以下、PETと略す)は、酸成分としてテレフタル酸残
基を80重量%以上含み、グリコール成分としてエチレン
グリコール残基を80重量%以上含むポリエステルである
が、場合により残りの成分が種類の異なるモノマーとの
共重合体あるいはブレンド物であってもよい。また、使
用するポリマー中には、重合段階でリン酸、亜リン酸お
よびそれらのエステルならびに無機粒子(シリカ、カオ
リン、炭酸カルシウム、リン酸カルシウム、二酸化チタ
ンなど)が含まれていてもよいし、重合後ポリマーに無
機粒子などがブレンドされていてもよい。
Polyethylene terephthalate (hereinafter abbreviated as PET) used in the present invention is a polyester containing 80% by weight or more of terephthalic acid residues as an acid component and 80% by weight or more of ethylene glycol residues as a glycol component. Therefore, the remaining components may be copolymers or blends with different types of monomers. Further, the polymer to be used may contain phosphoric acid, phosphorous acid and their esters and inorganic particles (silica, kaolin, calcium carbonate, calcium phosphate, titanium dioxide, etc.) at the polymerization stage, or after polymerization. Inorganic particles and the like may be blended with the polymer.

次にフィルムの製造方法を説明する。まず上記のPETポ
リマーを十分乾燥後、例えば280〜290℃の温度範囲にコ
ントロールした押出機、フィルターおよび口金を通じて
シート状に溶融成型し、回転する冷却ドラム上にキャス
トして急冷固化したフィルムを得る。この急冷固化した
フィルムは実質的に非晶状態(以下Aフィルムと称す
る)である。このAフィルムは共押出により積層された
フィルムでもよい。
Next, a method for producing the film will be described. First, after the PET polymer is sufficiently dried, it is melt-molded into a sheet shape through an extruder, a filter and a die which are controlled in a temperature range of 280 to 290 ° C., and cast on a rotating cooling drum to obtain a rapidly solidified film. . This rapidly solidified film is in a substantially amorphous state (hereinafter referred to as A film). The A film may be a film laminated by coextrusion.

次にAフィルムを通常100℃以上に十分予熱後、Δnが
1.0×10-3〜2.5×10-2となるような延伸倍率で第1延伸
を行なう(以下、このフィルムをB-1フィルムと称す
る)。Δnが上記範囲内に入る第1延伸倍率は、予熱温
度にもよるが、1.2〜4.0倍の範囲であり、予備試験によ
り容易に決定できる。B-1フィルムのΔnが、1.0×10-3
未満では、後の工程を最適化しても、厚み均一性に劣る
上、縦延伸倍率の向上が望めない。また、2.5×10-2
超えると、後の工程の結晶化の進行が著しく、横延伸時
の破れが多発して、安定製造条件が得られないので好ま
しくない。B-1フィルムのΔnは、好ましくは1.0×10-3
〜1.0×10-2の範囲である。
Next, after preheating A film to 100 ℃ or more, Δn
First stretching is performed at a stretching ratio of 1.0 × 10 −3 to 2.5 × 10 −2 (hereinafter, this film is referred to as B-1 film). The first draw ratio in which Δn falls within the above range is 1.2 to 4.0 times, depending on the preheating temperature, and can be easily determined by preliminary tests. Δn of B-1 film is 1.0 × 10 -3
When it is less than 1, even if the subsequent steps are optimized, the thickness uniformity is poor, and improvement in the longitudinal stretching ratio cannot be expected. On the other hand, if it exceeds 2.5 × 10 -2 , the crystallization in the subsequent step remarkably progresses, and breakage frequently occurs during transverse stretching, and stable production conditions cannot be obtained, which is not preferable. Δn of B-1 film is preferably 1.0 × 10 −3
The range is from 1.0 x 10 -2 .

第1延伸の延伸段数は、1段でもよいが、もちろん2段
以上の多段延伸でもよい。第1延伸を何段で行なうか
は、目的とする第1延伸倍率にもよるが、通常は1〜4
段、好ましくは1〜3段である。第1延伸の各延伸開始
点は、駆動された非粘着ロールと非粘着ニップロールで
構成されることが好ましく、第1延伸の間でフィルムは
ガラス転移温度以下にならないようにすることが好まし
い。
The number of stretching steps in the first stretching may be one, but of course it may be multi-stage stretching of two or more steps. The number of stages of the first stretching depends on the intended first stretching ratio, but usually 1 to 4
Stages, preferably 1 to 3 stages. Each stretching start point of the first stretching is preferably constituted by a driven non-adhesive roll and a non-adhesive nip roll, and it is preferable that the film does not fall below the glass transition temperature during the first stretching.

以上のようにして得られた、B-1フィルムをガラス転移
点温度以下に冷却することなく、複屈折率が、3.0×10
-2〜8.0×10-2となるように延伸倍率を1.0〜3.5の範囲
で調節し、1段又は多段で第2延伸する(以下、このフ
ィルムをB-2フィルムと称する)。このとき、フィルム
の温度は通常、100〜130℃の範囲である。
Obtained as described above, without cooling the B-1 film below the glass transition temperature, the birefringence is 3.0 × 10
The stretching ratio is adjusted in the range of 1.0 to 3.5 so as to be −2 to 8.0 × 10 −2 and the second stretching is performed in one step or multiple steps (hereinafter, this film is referred to as B-2 film). At this time, the temperature of the film is usually in the range of 100 to 130 ° C.

フィルムの温度が100℃未満では、延伸フィルムの厚み
斑が改良されない。一方、130℃を超えると、フィルム
の結晶化が進行して、フィルム表面が粗面化したり、横
延伸性が悪化するため不適当である。また、B-2フィル
ムの複屈折率が3.0×10-2未満では、延伸フィルムの厚
さ斑が良化しないため不適当であり、B-2フィルムの複
屈折率が8.0×10-2を超える場合には、B-2フィルムの結
晶化が進行し過ぎるため、かえって厚み均一性の改良効
果が弱く、かつ横延伸性が悪化するので好ましくない。
好ましくは3.0×10-2〜6.0×10-2、更に好ましくは、4.
0×10-2〜5.5×10-2の範囲である。かくして得られたフ
ィルムの平均屈折率()は1.570〜1.600の範囲である
ことが好ましい。1.570未満では、次の工程で縦延伸し
ても厚さの均一性が得られず好ましくない。一方、1.60
0を超えると、横延伸性が極端に悪化するため好ましく
ない。
If the temperature of the film is less than 100 ° C, the uneven thickness of the stretched film is not improved. On the other hand, if it exceeds 130 ° C., crystallization of the film proceeds, the surface of the film becomes rough, and the transverse stretchability deteriorates, which is not suitable. Further, if the birefringence of the B-2 film is less than 3.0 × 10 -2, it is unsuitable because the thickness unevenness of the stretched film does not improve, and the birefringence of the B-2 film is 8.0 × 10 -2 . If it exceeds the above range, the crystallization of the B-2 film will proceed too much, so that the effect of improving the thickness uniformity will be rather weak and the transverse stretchability will be deteriorated, which is not preferable.
Preferably 3.0 × 10 -2 to 6.0 × 10 -2 , more preferably 4.
It is in the range of 0 × 10 -2 to 5.5 × 10 -2 . The average refractive index () of the film thus obtained is preferably in the range of 1.570 to 1.600. If it is less than 1.570, the thickness uniformity cannot be obtained even if the film is longitudinally stretched in the next step, which is not preferable. On the other hand, 1.60
When it exceeds 0, the transverse stretchability is extremely deteriorated, which is not preferable.

かくして得られたB-2フィルムは、次にフィルム温度を
第2延伸におけるフィルム温度未満でかつ(95-250・Δ
n)〜(130-250・Δn)℃の範囲、好ましくは第2延
伸におけるフィルム温度未満でかつ(105-250・Δn)
〜(120-250・Δn)℃の範囲(ここでΔnとはフィル
ムの縦方向の延伸後、横方向の延伸前における複屈折率
を示す)とし、最終的な総合縦延伸倍率が4〜9倍の範
囲となる倍率で第3延伸する(以下、このフィルムをB-
3フィルムと称する)。かかる倍率が4.0未満では延伸倍
率の向上が達成されず、本発明の目的に合致しない。一
方、9.0を超えるとフィルムの両縁部の熱結晶化が進み
過ぎ、縦裂けし易いフィルムとなり、後の横延伸が困難
となるため好ましくない。総合延伸倍率が、4〜9倍の
範囲であれば、第3延伸の延伸段数に限定はない。また
第3延伸の延伸温度が前記温度範囲外では厚さ斑が悪化
し、好ましくない。
The B-2 film thus obtained then has a film temperature below the film temperature in the second stretching and (95-250
n) to (130-250 · Δn) ° C., preferably below the film temperature in the second stretching and (105-250 · Δn)
In the range of (120-250 · Δn) ° C. (where Δn is the birefringence of the film after stretching in the machine direction and before stretching in the cross direction), and the final total longitudinal stretching ratio is 4 to 9 Third stretch at a draw ratio that is in the range of (2)
3 film). If the draw ratio is less than 4.0, the improvement of the draw ratio is not achieved and the object of the present invention is not met. On the other hand, when it exceeds 9.0, thermal crystallization of both edges of the film proceeds too much, resulting in a film that is likely to be longitudinally torn, and it becomes difficult to laterally stretch the film later, which is not preferable. There is no limitation on the number of stretching steps in the third stretching as long as the total stretching ratio is in the range of 4 to 9 times. Further, if the stretching temperature of the third stretching is out of the above temperature range, uneven thickness is deteriorated, which is not preferable.

以上の条件で縦延伸されたB-3フィルムを横方向に3.2倍
以上、延伸することによって2軸配向フィルムが得られ
るが、いわゆるバランスドタイプを製造するときには、
縦延伸後の複屈折率を0.040〜0.060の範囲とするのが好
ましい。
A biaxially oriented film can be obtained by stretching the B-3 film longitudinally stretched 3.2 times or more in the transverse direction under the above conditions. When a so-called balanced type is produced,
The birefringence after longitudinal stretching is preferably in the range of 0.040 to 0.060.

更に高強度のフィルムを得る場合には、0.060を超え0.1
20以下の範囲とする。
To obtain a higher strength film, 0.060 over 0.1
The range is 20 or less.

本発明の横延伸温度は通常、100〜140℃の範囲である。
かくして得られたフィルムは、そのまま130〜250℃の温
度範囲で熱処理してもよいが、必要に応じて80〜160℃
の温度範囲で1.2〜3.0倍、再度、縦及び/又は横方向に
延伸した後、熱処理を行なってもよい。
The transverse stretching temperature of the present invention is usually in the range of 100 to 140 ° C.
The film thus obtained may be heat-treated as it is in a temperature range of 130 to 250 ° C, but if necessary, 80 to 160 ° C.
In the temperature range of 1.2 to 3.0 times, the film may be stretched again in the machine direction and / or the transverse direction, and then heat treated.

本発明で得られるフィルムは、同一の原料で従来の延伸
処方を採用して得られる、同一の縦延伸強度を有するフ
ィルムと比較すると、易滑性、透明性、厚み均一性に優
れている。更に、高強力化フィルムの製造においては、
上記の総合特性が得られると共にフィルム破れを極めて
少なくすることができる。しかも高延伸倍率化が実施で
きるため、生産能力の向上、更にはコストダウンにも大
きく貢献できる。また、横延伸性に優れ、破断が少な
く、この点でも生産性の向上に寄与するものである。
The film obtained in the present invention is excellent in slipperiness, transparency and thickness uniformity as compared with a film having the same longitudinal stretching strength obtained by adopting a conventional stretching formula with the same raw material. Furthermore, in the production of high strength film,
The above-mentioned comprehensive characteristics can be obtained, and the film breakage can be extremely reduced. Moreover, since a higher draw ratio can be implemented, it can greatly contribute to the improvement of production capacity and further cost reduction. Further, it has excellent lateral stretchability and little breakage, which also contributes to improvement in productivity.

かくして得られるフィルムは、生産スピードが上がりか
つ製膜時の破断性も少なく生産性が高い上、厚み均一
性、寸法安定性、易滑性、透明性等フィルム物性にも優
れ、かつ高強度のフィルムも製造が容易であり、現在知
られている各種フィルム用途に適用可能である。つまり
磁気テープ用途等の磁気記録媒体用ベースフィルム、コ
ンデンサー用途等の電気絶縁体用ベースフィルムばかり
でなく、包装用フィルムとしても好適である。
The film thus obtained has high production speed and high productivity with little breakability during film formation, and also has excellent film physical properties such as thickness uniformity, dimensional stability, slipperiness, transparency, and high strength. The film is also easy to manufacture and is applicable to various currently known film applications. That is, it is suitable not only as a base film for a magnetic recording medium such as a magnetic tape, a base film for an electrical insulator such as a capacitor, but also as a packaging film.

本発明の方法は、特に好ましくは、0.5μm〜50μmの
厚さのフィルムの製造に適用される。また、必要に応じ
本方法の工程内で各種表面処理を施して、フィルム特性
を改良することも好ましい。
The method of the invention is particularly preferably applied to the production of films with a thickness of 0.5 μm to 50 μm. It is also preferable to perform various surface treatments in the process of the present method as needed to improve the film characteristics.

〔実施例〕〔Example〕

以下、実施例によって本発明を更に詳細に説明するが、
本発明はこれらの実施例のみに限定されるものではな
い。
Hereinafter, the present invention will be described in more detail with reference to Examples.
The invention is not limited to these examples only.

実施例1 ポリエチレンテレフタレートチップ(固有粘度0.60,平
均粒径0.02μmのAl2O3を0.3重量%および平均粒径0.7
μmの炭酸カルシウムを0.3重量%含有)を180℃で5時
間乾燥後、285℃でTダイからシート状に押出して45℃
に保たれた回転ドラム上で冷却固化して、幅350mmの未
延伸非晶質フィルムを得た。その際、公知の静電密着法
を用いた。
Example 1 Polyethylene terephthalate chips (0.3 wt% of Al 2 O 3 having an intrinsic viscosity of 0.60 and an average particle size of 0.02 μm and an average particle size of 0.7)
(containing 0.3% by weight of calcium carbonate of μm) is dried at 180 ° C for 5 hours, and then extruded into a sheet form from a T die at 285 ° C to 45 ° C.
It was cooled and solidified on a rotating drum kept at 40 ° C. to obtain an unstretched amorphous film having a width of 350 mm. At that time, a known electrostatic contact method was used.

得られた未延伸非晶質フィルムを、多段のニップロール
の周速差を利用して、まず縦方向に第1延伸としてフィ
ルム温度112℃で1.6倍延伸後、連続して縦方向に第2延
伸として、フィルム温度110℃で2.8倍延伸した。
The obtained unstretched amorphous film is first stretched in the longitudinal direction as a first stretch by 1.6 times at a film temperature of 112 ° C. and then continuously stretched in the longitudinal direction to a second stretch using the peripheral speed difference of multi-stage nip rolls. The film was stretched 2.8 times at a film temperature of 110 ° C.

第1延伸後のフィルムの複屈折率は3.0×10-3であり、
第2延伸後のフィルム複屈折率については、4.2×10-2
であった。
The birefringence of the film after the first stretching is 3.0 × 10 −3 ,
The birefringence of the film after the second stretching is 4.2 × 10 -2
Met.

かくして得られたフィルムは更にフィルム温度を98℃と
して、1.22倍で、第3延伸を行なった。
The film thus obtained was further subjected to third stretching at a film temperature of 98 ° C. and 1.22 times.

得られた縦延伸フィルムの複屈折率Δnは0.063であっ
た。
The birefringence index Δn of the obtained longitudinally stretched film was 0.063.

次にテンター内で、108℃で横方向に3.9倍延伸し、更に
215℃で緊張熱固定を行ない、最終フィルム厚15μmの
フィルムを巻き取った。
Next, in the tenter, draw 3.9 times in the transverse direction at 108 ° C, and
Tension heat setting was performed at 215 ° C., and a film having a final film thickness of 15 μm was wound up.

実施例2 第3延伸を90℃で1.32倍とする以外は実施例1と同様に
延伸製膜した。
Example 2 A stretched film was formed in the same manner as in Example 1 except that the third stretching was performed at 90 ° C. to 1.32 times.

実施例3 第3延伸を85℃で1.53倍とする以外は実施例1と同様に
延伸製膜し、厚さ9μmのフィルムを得た。
Example 3 Stretching was performed in the same manner as in Example 1 except that the third stretching was performed at 85 ° C. by 1.53 times to obtain a film having a thickness of 9 μm.

比較例1 実施例1において第3延伸を110℃で1.3倍とし、110℃
で横方向に3.9倍、延伸したが、破断が頻発した。
Comparative Example 1 In Example 1, the third stretching was performed at 110 ° C. by 1.3 times, and 110 ° C.
Although it was stretched 3.9 times in the transverse direction, it frequently broke.

比較例2 実施例1において第3延伸を73℃で1.15倍延伸したが、
厚さ斑が悪く横延伸できなかった。
Comparative Example 2 In Example 1, the third stretch was stretched 1.73 times at 73 ° C.,
The thickness unevenness was so bad that the film could not be transversely stretched.

以上、得られた結果をまとめて表1に示す。The results obtained above are summarized in Table 1.

〔発明の効果〕 本発明によれば、厚み均一性、透明性および易滑性に優
れた配向ポリエステルを容易に製造でき、また、その高
速製造も可能であり、本発明の工業的価値は高い。
[Effect of the Invention] According to the present invention, an oriented polyester excellent in thickness uniformity, transparency and slipperiness can be easily produced, and high-speed production thereof is also possible, and the industrial value of the present invention is high. .

───────────────────────────────────────────────────── フロントページの続き (72)発明者 三木 崇利 神奈川県横浜市緑区鴨志田町1000番地 ダ イアホイル株式会社中央研究所内 (56)参考文献 特開 昭54−8672(JP,A) 特開 昭59−67018(JP,A) 特開 昭58−78729(JP,A) 特開 昭57−57631(JP,A) 特開 昭59−140028(JP,A) 特公 昭52−33666(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Takatoshi Miki 1000, Kamoshida-cho, Midori-ku, Yokohama-shi, Kanagawa Daifoil Co., Ltd. Central Research Laboratory (56) Reference JP-A-54-8672 (JP, A) JP JP-A-59-67018 (JP, A) JP-A-58-78729 (JP, A) JP-A-57-57631 (JP, A) JP-A-59-140028 (JP, A) JP-B-52-33666 (JP , B2)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ポリエチレンテレフタレートを主成分とす
る、実質的に非晶状態のフィルムを、縦方向に総合延伸
倍率4.0〜9.0倍で延伸した後、横方向に3.2倍以上で延
伸して配向フィルムを製造する方法において、該縦方向
の延伸が、 (A)非晶状態のフィルムを延伸倍率1.2〜4.0倍で複屈
折率が1×10-3〜2.5×10-2となるように1段または多
段で縦延伸し、 (B)フィルム温度をガラス転移点以下に冷却すること
なく、延伸倍率1.1〜3.5倍で複屈折率が3.0×10-2〜8.0
×10-2となるように1段または多段で縦延伸し、 (C)フィルム温度を前記(B)工程のフィルム温度未
満かつ(95-250・Δn)〜(130-250・Δn)℃の範囲
(但しΔnは縦方向の延伸後、横方向の延伸前における
フィルムの複屈折率を示す)とし、1段または多段で縦
延伸する工程 からなることを特徴とするポリエステルフィルムの製造
方法。
1. An oriented film which comprises a polyethylene terephthalate as a main component and which is stretched in a longitudinal direction at a total draw ratio of 4.0 to 9.0 and then in a transverse direction at a draw ratio of 3.2 or more. In the longitudinal direction, the step of stretching (A) the amorphous film in a stretch ratio of 1.2 to 4.0 and a birefringence of 1 × 10 −3 to 2.5 × 10 −2. Alternatively, the film is longitudinally stretched in multiple stages, and (B) the film has a birefringence of 3.0 × 10 -2 to 8.0 at a stretching ratio of 1.1 to 3.5 without cooling the film temperature below the glass transition point.
The film is longitudinally stretched in one step or in multiple steps so as to be × 10 -2, and (C) the film temperature is lower than the film temperature in the step (B) and (95-250 · Δn) to (130-250 · Δn) ° C. A method for producing a polyester film, comprising a step (where Δn represents a birefringence index of the film after stretching in the longitudinal direction and before stretching in the lateral direction), and performing longitudinal stretching in one step or in multiple steps.
JP33055988A 1988-12-27 1988-12-27 Method for producing polyester film Expired - Fee Related JPH0771822B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33055988A JPH0771822B2 (en) 1988-12-27 1988-12-27 Method for producing polyester film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33055988A JPH0771822B2 (en) 1988-12-27 1988-12-27 Method for producing polyester film

Publications (2)

Publication Number Publication Date
JPH02175130A JPH02175130A (en) 1990-07-06
JPH0771822B2 true JPH0771822B2 (en) 1995-08-02

Family

ID=18234005

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33055988A Expired - Fee Related JPH0771822B2 (en) 1988-12-27 1988-12-27 Method for producing polyester film

Country Status (1)

Country Link
JP (1) JPH0771822B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5233666B2 (en) 2008-12-26 2013-07-10 富士通株式会社 Life expectancy calculation device, portable terminal device, life expectancy calculation method, and life expectancy calculation program

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5233666B2 (en) 2008-12-26 2013-07-10 富士通株式会社 Life expectancy calculation device, portable terminal device, life expectancy calculation method, and life expectancy calculation program

Also Published As

Publication number Publication date
JPH02175130A (en) 1990-07-06

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