JP2569471B2 - Method for producing toughened polyester film - Google Patents

Method for producing toughened polyester film

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Publication number
JP2569471B2
JP2569471B2 JP22933585A JP22933585A JP2569471B2 JP 2569471 B2 JP2569471 B2 JP 2569471B2 JP 22933585 A JP22933585 A JP 22933585A JP 22933585 A JP22933585 A JP 22933585A JP 2569471 B2 JP2569471 B2 JP 2569471B2
Authority
JP
Japan
Prior art keywords
film
stretched
stretching
center
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP22933585A
Other languages
Japanese (ja)
Other versions
JPS6287321A (en
Inventor
晃一 阿部
武男 福山
俊哉 吉井
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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Filing date
Publication date
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Priority to JP22933585A priority Critical patent/JP2569471B2/en
Publication of JPS6287321A publication Critical patent/JPS6287321A/en
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は,強力化ポリエステルフイルムの製造方法に
関するものである。
The present invention relates to a method for producing a strengthened polyester film.

〔従来の技術〕 強力化ポリエステルフイルムの製造方法としては,た
とえば特公昭第35−5887号公報に示されているように,
いつたん二軸延伸したフイルムを,さらに延伸する方法
が知られている。
[Prior Art] As a method for producing a strengthened polyester film, for example, as disclosed in Japanese Patent Publication No. 35-5887,
A method of further stretching a film that has been biaxially stretched is known.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかし,最近では,さらに高強力化フイルムを得るた
めに再延伸倍率を高くすることが望まれているが,従来
の方法では安定した延伸ができず,製品収率が著しく悪
化するという欠点があつた。
Recently, however, it has been desired to increase the redrawing ratio in order to obtain a film with higher strength. However, there is a drawback in that the conventional method cannot perform stable drawing and the product yield is significantly deteriorated. Was.

本発明は,上記欠点を解消せしめ,高倍率の再延伸が
安定して行なえる強力化ポリエステルフイルムの製造方
法を提供せんとすることを目的とするものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a strengthened polyester film which can solve the above-mentioned drawbacks and can stably perform high-magnification redrawing.

〔問題点を解決するための手段〕[Means for solving the problem]

本発明は未延伸フイルムを,縦方向(フイルムの流れ
方向)に延伸後,横方向に延伸し,次いで,少なくとも
一方向に再延伸するフイルムの製造方法において,横延
伸されるフイルム端部の温度を,フイルム中央部の温度
より2℃以上低くして,クリツプ把持位置からフイルム
中央へ向けて10〜150mmの範囲の部分の複屈折が0.05〜
0.20で,かつ,その範囲の平均厚さがフイルム中央の厚
さの3〜15倍となるように横方向に延伸することを特徴
とする強力化ポリエステルフイルムの製造方法としたも
のである。
The present invention relates to a method for producing a film in which an unstretched film is stretched in a longitudinal direction (a film flow direction), then stretched in a transverse direction, and then re-stretched in at least one direction. Is lower than the temperature at the center of the film by 2 ° C or more, and the birefringence in the range of 10 to 150 mm from the gripping position toward the center of the film is 0.05 to
A method for producing a strengthened polyester film, characterized in that the film is stretched in the transverse direction so that the thickness is 0.20 and the average thickness in the range is 3 to 15 times the thickness at the center of the film.

本発明に用いるポリエステルは,芳香族ジカルボン酸
(またはそのエステル)とジオキシ化合物を重縮合して
得られる熱可塑性ポリエステルであれば,とくに限定さ
れないが,本発明による延伸性向上効果がとくに顕著な
のは,ポリエチレンテレフタレート,ポリエチレン−
α,β−ビス(2−クロルフエノキシ)エタン−4,4′
−ジカルボキシレート,ポリエチレン−2,6−ナフタレ
ートなどを主成分とするガラス転移点が70℃以上の剛直
ポリエステルであり,その中でも,特に本発明の効果が
大きいのは,ポリエチレン−α,β−ビス(2−クロル
フエノキシ)エタン−4,4′−ジカルボキシレートを主
成分とするポリエステルである。
The polyester used in the present invention is not particularly limited as long as it is a thermoplastic polyester obtained by polycondensation of an aromatic dicarboxylic acid (or an ester thereof) and a dioxy compound, but the effect of improving the stretchability according to the present invention is particularly remarkable. Polyethylene terephthalate, polyethylene
α, β-bis (2-chlorophenoxy) ethane-4,4 ′
Rigid polyesters having a glass transition point of 70 ° C. or higher containing dicarboxylate, polyethylene-2,6-naphthalate and the like as main components. Among them, polyethylene-α, β- Polyester containing bis (2-chlorophenoxy) ethane-4,4'-dicarboxylate as a main component.

また,本発明に用いるポリエステルに,本発明の目的
を阻害しない範囲で,他種ポリマをブレンドしてもよい
し,また酸化防止剤,熱安定剤,表面突起形成剤,核生
成剤,紫外線吸収剤などの無機または有機添加剤を通常
添加される量程度添加してもよい。
The polyester used in the present invention may be blended with other polymers as long as the object of the present invention is not impaired, or may be an antioxidant, a heat stabilizer, a surface projection forming agent, a nucleating agent, an ultraviolet absorbing agent. An inorganic or organic additive such as an agent may be added in an amount that is usually added.

また,本発明に用いるポリエステルの溶融粘度は特に
限定されないが,溶融粘度が500〜20000ポイズ,特に70
0〜10000ポイズの範囲である場合が,延伸性,得られた
フイルムのヤング率がより一層良好となるので,特に好
ましい。
Although the melt viscosity of the polyester used in the present invention is not particularly limited, the melt viscosity is 500 to 20,000 poise, and
A range of 0 to 10,000 poise is particularly preferred because stretchability and Young's modulus of the obtained film are further improved.

本発明に用いる二軸延伸フイルムを安定して製造する
には,次の方法が有効である。
The following method is effective for stably producing the biaxially stretched film used in the present invention.

上記のポリエステルのペレツトを公知の溶融押出機を
用いてシート状に押出し,冷却固化して未延伸フイルム
を作る。
The above-mentioned polyester pellets are extruded into a sheet using a known melt extruder, and cooled and solidified to produce an unstretched film.

この未延伸フイルムを,長手方向に2.5〜4.0倍,好ま
しくは3.0〜3.8倍延伸する。延伸倍率を上記範囲にする
と,複屈折0.05〜0.20の部分を10〜150mm有する二軸延
伸フイルムが得られやすくなる。また,延伸温度は,ポ
リマのガラス転移点をTgとした場合,Tg−20℃〜Tg+35
℃の範囲,延伸速度は103〜106%/分の範囲が好適であ
る。
The unstretched film is stretched 2.5 to 4.0 times, preferably 3.0 to 3.8 times in the longitudinal direction. When the stretching ratio is in the above range, a biaxially stretched film having a portion having a birefringence of 0.05 to 0.20 of 10 to 150 mm is easily obtained. The stretching temperature is Tg-20 ° C to Tg + 35, where Tg is the glass transition point of the polymer.
C. and the stretching speed are preferably in the range of 10 3 to 10 6 % / min.

ここで,この一軸延伸フイルムの結晶化度を15〜30%
とすると,複屈折0.05〜0.20の部分を10〜150mm幅有す
る二軸延伸フイルムがより一層得られやすくなるので好
適である。
Here, the crystallinity of this uniaxially stretched film is 15 to 30%.
This is preferable because a biaxially stretched film having a portion having a birefringence of 0.05 to 0.20 and a width of 10 to 150 mm is more easily obtained.

次に,この一軸延伸フイルムをステンタを用いて,幅
方向に2.3〜4.0倍,好ましくは2.5〜3.8倍延伸する。延
伸倍率(ステンタの最大幅/ステンタの入口幅)を上記
の範囲にすると,複屈折0.05〜0.20の部分を10〜150mm
幅有し,かつ,該部分の平均厚さがフイルム中央の厚さ
の3〜1.5倍の厚さである二軸延伸フイルムが得られや
すくなる。また,この時の延伸温度は,ポリマの冷結晶
化温度をTccとした場合,そのTccとTgの差が45℃未満の
ポリエステルは,Tcc−15℃〜Tcc+15℃,TccとTgの差が4
5℃以上のポリエステルは,Tcc−60℃〜Tccの範囲が好適
である。
Next, the uniaxially stretched film is stretched 2.3 to 4.0 times, preferably 2.5 to 3.8 times in the width direction using a stenter. If the draw ratio (maximum width of the stenter / width of the entrance of the stenter) is within the above range, the portion with a birefringence of 0.05 to 0.20 is 10 to 150 mm.
It is easy to obtain a biaxially stretched film having a width and an average thickness of the portion being 3 to 1.5 times the thickness of the center of the film. As for the stretching temperature at this time, when the cold crystallization temperature of the polymer is Tcc, polyester having a difference between Tcc and Tg of less than 45 ° C is Tcc-15 ° C to Tcc + 15 ° C, and the difference between Tcc and Tg is 4 ° C.
The polyester having a temperature of 5 ° C. or more preferably has a range of Tcc−60 ° C. to Tcc.

またクリツプの温度をTg+100℃以下とし,クリツプ
把持位置から中央に向つて10mmの範囲の部分の温度をフ
イルム中央より2℃,好ましくは4℃,さらに好ましく
は10℃以上低くすることが必要である。また,延伸速度
は103〜105%/分の範囲が好適である。
In addition, the temperature of the clip must be Tg + 100 ° C or less, and the temperature of a portion within a range of 10mm from the clip holding position toward the center must be lower than the film center by 2 ° C, preferably 4 ° C, more preferably 10 ° C or more. . The stretching speed is preferably in the range of 10 3 to 10 5 % / min.

次に,この二軸延伸フイルムを120〜180℃の範囲の温
度で,幅方向に,原長に対し3〜30%弛緩させつつ,0.5
〜120秒間熱処理すると複屈折0.05〜0.20の部分を10〜1
50mm有し,かつ,該部分の平均厚さがフイルム中央の3
〜15倍である二軸延伸フイルムが,より一層得られやす
くなる。
Next, the biaxially stretched film is relaxed in the width direction at a temperature in the range of 120 to 180 ° C. by 3 to 30% with respect to the original length, while being 0.5 mm apart.
After heat treatment for ~ 120 seconds, the part with birefringence of 0.05 ~ 0.20 becomes 10 ~ 1
50mm, and the average thickness of the part is 3mm at the center of the film.
It is easier to obtain a biaxially stretched film of up to 15 times.

ここで,この二軸延伸フイルムは,エツジのクリツプ
把持位置からフイルム中央へ向かつて,複屈折が0.05〜
0.20の範囲の部分を10〜150mm幅,好ましくは15〜100mm
幅,さらに好ましくは20〜80mm幅有することが必要であ
る。該部分の幅が上記の範囲より狭いと,これを再延伸
する場合の延伸性が不良となるので好ましくない。ま
た,該部分の幅が上記範囲より広いと,得られた強力化
フイルムの幅が狭くなり,生産収率が低くなるので好ま
しくない。
Here, the biaxially stretched film has a birefringence of 0.05 to less from the clip holding position of the edge toward the center of the film.
A part in the range of 0.20 is 10 to 150 mm width, preferably 15 to 100 mm
It must have a width, more preferably a width of 20 to 80 mm. If the width of the portion is smaller than the above range, the stretchability when re-stretching the portion is not preferable, which is not preferable. On the other hand, if the width of the portion is wider than the above range, the width of the obtained strengthened film is reduced, and the production yield is undesirably reduced.

また,上記の複屈折の範囲の部分の厚さを連続して測
定して得られた平均厚さは,フイルム中央部の厚さの3
〜15倍,好ましくは3.5〜12倍,さらに好ましくは4〜1
0倍であることが必要である。この値が上記範囲より小
さくても,また,大きくても再延伸する場合の延伸性が
不良となるので好ましくない。
The average thickness obtained by continuously measuring the thickness in the above-mentioned range of birefringence is 3% of the thickness at the center of the film.
~ 15 times, preferably 3.5 ~ 12 times, more preferably 4 ~ 1
Must be 0 times. If this value is smaller or larger than the above range, the stretchability in the case of re-stretching becomes unfavorable because it becomes poor.

また,この二軸延伸フイルムのエツジのクリツプ把持
位置からフイルム中央へ向つて5mmの部分の長手方向屈
折率比を1.03〜1.08,密度指数を0.01〜0.04の範囲にす
ると,これを再延伸する場合の延伸性がより一層良好と
なるので望ましい。
If the longitudinal refractive index ratio of the part of 5 mm from the edge gripping position of the edge of the biaxially stretched film toward the film center is in the range of 1.03 to 1.08 and the density index is in the range of 0.01 to 0.04. Is preferable because the stretchability of the film becomes even better.

以上の説明をわかりやすくするために,クリツプの把
持状態を模式的に示した図面で説明する。
In order to make the above description easy to understand, a description will be given with reference to the drawings schematically showing the gripping state of the clip.

第1図はフイルムをクリツプが把持している状態の平
面図であり,1はクリツプ,4はフイルムであり,はフイ
ルム中央部,特にフイルムの幅方向の中央である。
FIG. 1 is a plan view of a state in which a clip is gripping a film, 1 is a clip, 4 is a film, and is a center of the film, especially a center in the width direction of the film.

第2図は第1図におけるA−A′の断面図である。
がクリツプ把持位置であり,Wが複屈折が0.05〜0.20の部
分の幅であり,Wを10〜150mmとすることが本発明では必
須となる。また,l0はフイルム中央部の厚さであり,W
の幅の部分の平均厚さがl0の3〜15倍であることが本発
明では必須となる。
FIG. 2 is a sectional view taken along the line AA 'in FIG.
Is the clip gripping position, W is the width of the portion where the birefringence is 0.05 to 0.20, and it is essential in the present invention that W is 10 to 150 mm. In addition, l 0 is the thickness of the film center, W
It is essential in the present invention that the average thickness of the part having the width of 3 is 3 to 15 times l0.

次に,この二軸延伸フイルムを長手方向,幅方向の少
なくとも一方向に再延伸する。この時の,長手方向の延
伸倍率α,幅方向の延伸倍率βが下式を満足するように
すれば,再延伸の延伸性がより一層良好となるので望ま
しい。
Next, the biaxially stretched film is stretched again in at least one of the longitudinal direction and the width direction. At this time, it is preferable that the stretching ratio α in the longitudinal direction and the stretching ratio β in the width direction satisfy the following expression, because the stretchability of the re-stretching is further improved.

2.2≦α+β≦8.0 なお,たとえば,長手方向にのみ再先伸する場合はβ
=1とする。
2.2 ≦ α 2 + β 2 ≦ 8.0 For example, when re-extending only in the longitudinal direction, β
= 1.

また,この時の延伸温度は120〜200℃,延伸速度は10
3〜106%/分の範囲が好適である。
The stretching temperature at this time is 120-200 ° C, and the stretching speed is 10
A range of 3 to 10 6 % / min is preferred.

次に必要に応じて,再延伸された二軸延伸フイルムを
再熱処理することもできる。この場合の熱処理条件は特
に限定されないが,温度180〜260℃,好ましくは200〜2
40℃で,時間0.5〜120秒間,好ましくは1.0〜60秒間と
することが,得られたフイルムのヤング率の点で好適で
ある。
Next, if necessary, the re-stretched biaxially stretched film can be re-heat treated. The heat treatment conditions in this case are not particularly limited, but the temperature is 180 to 260 ° C., preferably 200 to 2 ° C.
A temperature of 40 ° C. for a time of 0.5 to 120 seconds, preferably 1.0 to 60 seconds is suitable from the viewpoint of the Young's modulus of the obtained film.

〔作用〕[Action]

本発明は,上述したように,二軸延伸フイルムのエツ
ジのクリツプ把持位置近傍の物性を特定化したので,再
延伸の際にエツジからの破断がおこりにくくなり,次の
ようなすぐれた効果が得られたものである。
As described above, the present invention specifies the physical properties of the edge of the biaxially stretched film in the vicinity of the clip holding position of the edge, so that the edge of the biaxially stretched film is less likely to break during re-stretching, and the following excellent effects are obtained. It is obtained.

〔発明の効果〕〔The invention's effect〕

本発明製造法によれば,二軸延伸フイルムを少なくと
も一方向に再延伸するに際し,再延伸倍率を高くしても
フイルム破れがおこりにくく,高ヤング率フイルムを安
定して収率良く,製造することが可能となる。得られた
フイルムは磁気テープベースやコンデンサ用として有用
である。
According to the production method of the present invention, when re-stretching a biaxially stretched film in at least one direction, even if the re-drawing ratio is increased, the film is hardly broken, and a film having a high Young's modulus can be produced stably with a high yield. It becomes possible. The resulting film is useful for magnetic tape bases and capacitors.

〔測定および評価方法〕[Measurement and evaluation methods]

(1)延伸性 再延伸製膜操作を48時間連続して行ない,その間に生
じたフイルムの破れが0〜1回の範囲である場合は延伸
性良好,破れが2回以上生じた場合は延伸性不良と判定
した。
(1) Stretchability A re-stretching film-forming operation is performed continuously for 48 hours. The film is good in stretchability when the film tears during that time is in the range of 0 to 1 time, and is stretched when tears occur 2 or more times. It was judged as poor sex.

(2)屈折率 ナトリウムD線(波長589nm)を光源として,アツベ
屈折計を用いて測定した。なお,マウント液にはヨウ化
メチレンまたはイオウ−ヨウ化メチレン溶液を用い,25
℃・65%RHにて測定した。
(2) Refractive index Using a sodium D line (wavelength: 589 nm) as a light source, the refractive index was measured using an Atsube refractometer. Use methylene iodide or a sulfur-methylene iodide solution as the mounting solution.
It was measured at 65 ° C. and 65% RH.

(3)複屈折 上記の方法で,試料の長手方向と幅方向の屈折率を測
定し,(長手方向−幅方向)の差をもつて複屈折とし
た。
(3) Birefringence The refractive index in the longitudinal direction and the width direction of the sample was measured by the above-mentioned method, and the sample was defined as birefringence with a difference of (longitudinal direction-width direction).

(4)長手方向屈折率比 上記(2)の方法で試料の長手方向の屈折率(Aとす
る)および溶融プレス後10℃の水中へ急冷して作つた無
配向(アモルフアス)フイルムの長手方向の屈折率(B
とする)を測定し,A/Bをもつて,長手方向屈折率比とし
た。
(4) Longitudinal refractive index ratio The longitudinal refractive index (A) of the sample and the longitudinal direction of a non-oriented (amorphous) film made by quenching into 10 ° C water after melt-pressing by the method of (2) above. Index of refraction (B
Was measured, and A / B was taken as the longitudinal refractive index ratio.

(5)密度および密度指数 四塩化炭素とn−ヘプタンからなる密度勾配管を用い
て試料の密度(ρとする)および溶融プレス後10℃の水
中に急冷して作つた無配向(アモルフアス)フイルムの
密度(ρとする)を測定し,ρ−ρをもつて密度指
数とした。なお測定は25℃にて行なつた。なお,結晶化
度は密度から計算した。
(5) Density and density index Using a density gradient tube composed of carbon tetrachloride and n-heptane, the density of the sample (referred to as ρ) and a non-oriented (amorphous) film made by quenching in water at 10 ° C after melt pressing. (Ρ 0 ) was measured, and ρ−ρ 0 was used as the density index. The measurement was performed at 25 ° C. The crystallinity was calculated from the density.

(6)溶融粘度 島津高化式フローテスターを用いて290℃,ずり速度2
00sec-1にて測定した。
(6) Melt viscosity Using a Shimadzu Koka type flow tester, 290 ° C, shear rate 2
It was measured at 00 sec -1 .

(7)フイルムのヤング率 ASTM−D−882に規定された方法にしたがつて,イン
ストロンタイプの引張試験機を用いて,25℃・65%RHに
て測定した。
(7) Young's modulus of film Measured at 25 ° C. and 65% RH using an Instron type tensile tester according to the method specified in ASTM-D-882.

(8)ガラス転移点Tg冷結晶化温度Tcc パーキンエルマー社製のDSC(示差走査熱量計)II型
を用いて測定した。DSCの測定条件は次のとおりであ
る。すなわち,試料ポリマ10mgをDSC装置にセツトし
(融点+30℃)の温度で5分間溶融した後,液体窒素中
に急冷する。この急冷試料を10℃/分で昇温し,ガラス
転移点Tgを検知する。さらに昇温を続け,ガラス状態か
らの結晶化の発熱ピーク温度をもつて冷結晶化温度Tcc
とする。
(8) Glass transition point Tg Cold crystallization temperature Tcc Measured using a DSC (differential scanning calorimeter) type II manufactured by PerkinElmer. The measurement conditions of the DSC are as follows. That is, 10 mg of a sample polymer is set in a DSC apparatus, melted at a temperature of (melting point + 30 ° C.) for 5 minutes, and then rapidly cooled in liquid nitrogen. The quenched sample is heated at a rate of 10 ° C./min, and the glass transition point Tg is detected. The temperature is further increased and the crystallization temperature from the glassy state is reached.
And

〔実施例〕〔Example〕

以下に本発明の実施例を述べるが,本発明はこれらの
実施例によつて限定されるものではない。
Examples of the present invention will be described below, but the present invention is not limited to these examples.

実施例1〜2,比較例1〜3 ポリエチレンα,β−ビス(2−クロルフエノキシ)
エタン4,4′−ジカルボキシレートのペレツト(溶融粘
度:2600ポイズ)を,180℃で3時間減圧乾燥(3Torr)さ
せた。これを押出機(スクリュー径:40mmφ)に供給し,
300℃でシート状に溶融押出し,静電印加キヤスト法に
て表面温度20℃のキヤステイング・ドラムに巻きつけて
冷却固化し,フイルム中央部の厚さ約105μmの未延伸
フイルムを作つた。この未延伸フイルムを延伸温度115
℃で長手方向に3.4倍延伸した。この延伸は2組のロー
ルの周速差によつて行なわれ,延伸速度は10000%/分
であつた。この一軸延伸フイルムをステンタを用いて,
延伸速度2000%/分で幅方向に3.8倍延伸した。延伸温
度は130℃であつた。ただし,クリツプ温度は50℃,ク
リツプ把持部から中央へ向つて10mmの領域の温度は115
℃となるようにステンタ内に熱風遮断板およびクリツプ
冷却水装置を設けた。さらに,この二軸延伸フイルム
を,幅方向に原長の5%だけ弛緩させつつ,160℃で10秒
間熱処理した。
Examples 1-2, Comparative Examples 1-3 Polyethylene α, β-bis (2-chlorophenoxy)
A pellet of ethane 4,4'-dicarboxylate (melt viscosity: 2600 poise) was dried under reduced pressure (3 Torr) at 180 ° C. for 3 hours. This is supplied to an extruder (screw diameter: 40 mmφ),
The film was melt-extruded at 300 ° C into a sheet, wound around a casting drum with a surface temperature of 20 ° C by an electrostatic application casting method, cooled and solidified, and an unstretched film having a thickness of about 105 μm at the center of the film was produced. The unstretched film is stretched at a stretching temperature of 115.
The film was stretched 3.4 times in the longitudinal direction at ° C. The stretching was performed by a difference in peripheral speed between two sets of rolls, and the stretching speed was 10,000% / min. Using this uniaxially stretched film with a stenter,
The film was stretched 3.8 times in the width direction at a stretching speed of 2000% / min. The stretching temperature was 130 ° C. However, the clip temperature is 50 ° C, and the temperature in the area of 10 mm from the clip gripper toward the center is 115 ° C.
A hot air shut-off plate and a clip cooling water device were provided in the stenter so that the temperature became ℃. Further, the biaxially stretched film was heat-treated at 160 ° C. for 10 seconds while relaxing in the width direction by 5% of the original length.

こうして得られた二軸延伸フイルムは,エツジのクリ
ツプ把持位置からフイルム中央へ向つて,複屈折が0.05
〜0.20の範囲の部分の幅が35mmであり,また,この部分
の厚さの平均値は65μmであり,フイルム中央部の7.6
倍であつた(第1表・実施例1)。
The biaxially stretched film thus obtained has a birefringence of 0.05 from the edge of the clip to the center of the film.
The width of the part in the range of .about.0.20 is 35 mm, and the average value of the thickness of this part is 65 μm.
It was doubled (Table 1 and Example 1).

また,フイルムの製造条件を変更して種々の二軸延伸
フイルムを作つた(第1表・実施例2,比較例1〜3)。
In addition, various biaxially stretched films were produced by changing the film production conditions (Table 1, Example 2, Comparative Examples 1 to 3).

これらのフイルムを,延伸温度190℃で長手方向に1.8
倍延伸した。この延伸は2組のロールの周速差によつて
行なわれ,延伸速度は50000%/分であつた。
These films are stretched at a stretching temperature of 190 ° C in the longitudinal direction for 1.8
It was stretched twice. This stretching was performed by a difference in peripheral speed between two sets of rolls, and the stretching speed was 50,000% / min.

この時の延伸性は,第1表に示したとおり,製造方法
が本発明範囲の場合(実施例1〜2)は,良好であり,
高ヤング率の強力化フイルムを安定して製造できた。し
かし,製造方法が本発明外である場合には,延伸性が不
良であり,安定した製造ができなかつた(比較例1〜
3)。
As shown in Table 1, the stretchability at this time was good when the production method was within the scope of the present invention (Examples 1 and 2).
A high-strength film with a high Young's modulus was produced stably. However, when the production method was outside the present invention, the stretchability was poor and stable production was not possible (Comparative Examples 1 to 4).
3).

実施例3〜4,比較例4〜6 ポリエチレンテレフタレートのペレツト(溶融粘度:1
700ポイズ)を,180℃で3時間減圧乾燥(3Torr)させ
た。これを押出機(スクリュー径:40mmφ)に供給し,30
0℃でシート状に溶融押出し,静電印加キヤスト法にて
表面温度20℃のキヤステイング・ドラムに巻きつけて冷
却固化し,フイルム中央部の厚さ約105μmの未延伸フ
イルムを作つた。
Examples 3-4, Comparative Examples 4-6 Pellet of polyethylene terephthalate (melt viscosity: 1
(700 poise) was dried under reduced pressure (3 Torr) at 180 ° C. for 3 hours. This is supplied to an extruder (screw diameter: 40 mmφ),
The film was melt-extruded at 0 ° C into a sheet, wound around a casting drum having a surface temperature of 20 ° C by the electrostatic application casting method, cooled and solidified, and an unstretched film having a thickness of about 105 μm at the center of the film was produced.

この未延伸フイルムを延伸温度80℃で長手方向に3.4
倍延伸した。この延伸は2組のロールの周速差によつて
行なわれ,延伸速度は10000%/分であつた。この一軸
延伸フイルムをステンタを用いて,延伸速度2000%/分
で幅方向に3.8倍延伸した。延伸温度は90℃であつた。
ただし,クリツプ温度は50℃,クリツプ把持位置からス
テンタ中央へ向つて10mmの領域の温度は80℃となるよう
にステンタ内に熱風遮断板およびクリツプ冷却水装置を
設けた。さらに,この二軸延伸フイルムを,幅方向に原
長の5%だけ弛緩させつつ,120℃で10秒間熱処理した。
This unstretched film is stretched at a stretching temperature of 80 ° C.
It was stretched twice. The stretching was performed by a difference in peripheral speed between two sets of rolls, and the stretching speed was 10,000% / min. The uniaxially stretched film was stretched 3.8 times in the width direction using a stenter at a stretching speed of 2000% / min. The stretching temperature was 90 ° C.
However, a hot air cut-off plate and a clip cooling water device were installed in the stenter so that the clip temperature was 50 ° C and the temperature in the area of 10 mm from the clip gripping position to the center of the stenter was 80 ° C. Further, the biaxially stretched film was heat-treated at 120 ° C. for 10 seconds while relaxing in the width direction by 5% of the original length.

こうして得られた二軸延伸フイルムは,エツジのクリ
ツプ把持位置からフイルム中央へ向つて,複屈折が0.05
〜0.20の範囲の部分の幅が20mmであり,また,この部分
の厚さの平均値は50μmであり,フイルム中央部の5.9
倍であつた(第2表・実施例3)。
The biaxially stretched film thus obtained has a birefringence of 0.05 from the edge of the clip to the center of the film.
The width of the part in the range of ~ 0.20 is 20 mm, and the average thickness of this part is 50 µm.
It was doubled (Table 2 and Example 3).

また,フイルムの製造条件を変更して種々の二軸延伸フ
イルムを作つた(第2表・実施例4,比較例4〜6)。
Further, various biaxially stretched films were produced by changing the film production conditions (Table 2, Example 4, Comparative Examples 4 to 6).

これらのフイルムを,同時二軸テンターを用いて,延
伸温度150℃で,長手方向,幅方向同時に1.5倍ずつ延伸
した。
These films were stretched 1.5 times simultaneously in the longitudinal and width directions at a stretching temperature of 150 ° C. using a simultaneous biaxial tenter.

この時の延伸性は,第2表に示したとおり,製造方法
が本発明範囲の場合(実施例3〜4)は,良好であり,
高ヤング率の強力化フイルムを安定して製造できた。し
かし,製造方法が本発明外である場合には,延伸性が不
良であり,安定した製造ができなかつた(比較例4〜
6)。
As shown in Table 2, the stretchability at this time was good when the production method was within the scope of the present invention (Examples 3 and 4).
A high-strength film with a high Young's modulus was produced stably. However, when the production method was outside the present invention, the stretchability was poor and stable production was not possible (Comparative Examples 4 to 5).
6).

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

第1図はフイルムをクリツプが把持している状態の平面
図,第2図は第1図におけるA−A′の断面図である。
図における番号,記号は次の通りである。 1:クリツプ、2:クリツプ支柱、3:クリツプ上部押え板、
4:フイルム、:フイルム中央部、:クリツプ把持位
置、W:複屈折が0.05〜0.20の部分の幅、l0:フイルム中
央部の厚さである。
FIG. 1 is a plan view showing a state in which the clip is gripping the film, and FIG. 2 is a sectional view taken along the line AA 'in FIG.
The numbers and symbols in the figure are as follows. 1: clip, 2: clip support, 3: clip upper holding plate,
4: Film: film center portion: clip gripping position, W: width of the portion of the birefringence 0.05 to 0.20, l 0: the thickness of the film center portion.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭55−37370(JP,A) 特開 昭55−34937(JP,A) 特開 昭58−224723(JP,A) 実開 昭62−35817(JP,U) ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-55-37370 (JP, A) JP-A-55-34937 (JP, A) JP-A-58-224723 (JP, A) 35817 (JP, U)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】未延伸フイルムを,縦方向に延伸後,横方
向に延伸し,次いで,少なくとも一方向に再延伸するフ
イルムの製造方法において,横延伸されるフイルム端部
の温度を,フイルム中央部の温度より2℃以上低くし
て,クリツプ把持位置からフイルム中央へ向けて10〜15
0mmの範囲の部分の複屈折が0.05〜0.20で,かつ,その
範囲の平均厚さがフイルム中央の厚さの3〜15倍となる
ように横方向に延伸することを特徴とする強力化ポリエ
ステルフイルムの製造方法。
An unstretched film is stretched in the machine direction, stretched in the transverse direction, and then re-stretched in at least one direction. Temperature lower than 2 ° C and move 10 to 15 from the gripping position toward the center of the film.
Strengthened polyester characterized in that it has a birefringence of 0.05 to 0.20 in a range of 0 mm and is stretched in the transverse direction so that the average thickness in the range is 3 to 15 times the thickness of the center of the film. Film manufacturing method.
JP22933585A 1985-10-15 1985-10-15 Method for producing toughened polyester film Expired - Lifetime JP2569471B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22933585A JP2569471B2 (en) 1985-10-15 1985-10-15 Method for producing toughened polyester film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22933585A JP2569471B2 (en) 1985-10-15 1985-10-15 Method for producing toughened polyester film

Publications (2)

Publication Number Publication Date
JPS6287321A JPS6287321A (en) 1987-04-21
JP2569471B2 true JP2569471B2 (en) 1997-01-08

Family

ID=16890541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22933585A Expired - Lifetime JP2569471B2 (en) 1985-10-15 1985-10-15 Method for producing toughened polyester film

Country Status (1)

Country Link
JP (1) JP2569471B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69526638T2 (en) * 1994-08-30 2002-12-12 Toray Industries BIAXIAL ORIENTED POLYESTER FILM AND THEIR PRODUCTION METHOD
KR101530805B1 (en) * 2011-05-06 2015-06-22 코니카 미놀타 가부시키가이샤 Stretched cellulose ester film and method for producing same
CN113580456B (en) * 2021-08-11 2023-03-24 浙江格尔泰斯环保特材科技股份有限公司 Preparation method of polytetrafluoroethylene microporous film

Also Published As

Publication number Publication date
JPS6287321A (en) 1987-04-21

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