JPS63162223A - Treating process of polyester film - Google Patents

Treating process of polyester film

Info

Publication number
JPS63162223A
JPS63162223A JP30869086A JP30869086A JPS63162223A JP S63162223 A JPS63162223 A JP S63162223A JP 30869086 A JP30869086 A JP 30869086A JP 30869086 A JP30869086 A JP 30869086A JP S63162223 A JPS63162223 A JP S63162223A
Authority
JP
Japan
Prior art keywords
polyester film
temperature
polyester
film
nitrogen
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
JP30869086A
Other languages
Japanese (ja)
Inventor
Kenji Tsunashima
研二 綱島
Seizo Aoki
青木 精三
Susumu Yanaga
彌永 進
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
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP30869086A priority Critical patent/JPS63162223A/en
Publication of JPS63162223A publication Critical patent/JPS63162223A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • B29C71/009After-treatment of articles without altering their shape; Apparatus therefor using gases without chemical reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2067/00Use of polyesters or derivatives thereof, as moulding material

Landscapes

  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Plasma & Fusion (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

PURPOSE:To obtain a film excellent in slit property by treating a polyester film in the mixed gas of carbon dioxide with nitrogen, and under pressure. CONSTITUTION:A polyester film is brought in contact with a gas mixed at 1/99-95/5 volume mixing ratio of carbon dioxide with nitrogen under high pressure of 20kg/cm<2>-10kg/cm<2>. As polyester, biaxially oriented and heat-trcated polyethylene terephthalate having especially 40% or more of crystallinity index and 0.03 or more degree of surface orientation, is preferable. As the mixed gas for treatment, the containing of nitrogen gas is essential condition, and if the content of nitrogen gas is not equal to 5% or more, preferably equal to 20% or more, the improvement of slit suitability is not expected. As the treatment temperature at this time, the temperature range from the temperature higher by 40 deg.C them the glass transition temperature (Tg) of polyester and at a cooling and crystallization temperature at the highest to the temperature lower by 40 deg.C than the Tg.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、ポリエステルフィルムの処理方法に関するも
の、ざらに詳しくは、主としてポリエステルフィルムの
スリット適性にすぐれたポリエステルフィルムの処理方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for processing a polyester film, and more specifically, to a method for processing a polyester film that has excellent slitting suitability.

[従来の技術] ポリエステルフィルムのスリット適性、すなわち、ポリ
エステルフィルムを一定の巾特に、10mm巾以下の小
中に切断するスリット工程で、該ポリエステルフィルム
の切断のしやすさ、すなわち切断面が凹凸やノコギリ刃
状になったり、ざらには切断面にヒゲやスリット片が付
着していたり、ひどいときには、スリット時にフィルム
が切断するという各種のトラブルを生じない時にはスリ
ット適性に優れているというが、従来までのポリエステ
ルフィルムではかかるスリット適正に劣り上記各種トラ
ベルを生じていた。このため、従来までは、スリットの
刃の種類や、きり方、ざらにはポリエステルフィルムを
加熱したり、冷却したりする工夫がなされていた。
[Prior Art] The slitting suitability of a polyester film, that is, the ease with which the polyester film can be cut in the slitting process in which the polyester film is cut into small pieces of a certain width, especially 10 mm or less, is determined, that is, whether the cut surface is uneven or uneven. It is said that it has excellent slitting suitability when it does not cause various troubles such as saw-toothed edges, hairs or slit pieces attached to the cut surface, or in severe cases, the film cuts during slitting. Previous polyester films had poor slit suitability, resulting in the various types of travel described above. For this reason, conventional methods have been used to change the type of slitting blade, the cutting method, and the roughness by heating or cooling the polyester film.

[発明が解決しようとする問題点] しかし、従来までの切断法を主とした改良では、スリッ
ト適正は、多少とも向上しても実用上の問題解決には至
らず、特に磁気記録用のベースフィルムのように、異物
、ゴミの付着や、フィルム端面のヒゲを好まない用途で
はスリット適正の悪いポ1)エステルフィルムは致命的
な欠点であった。
[Problems to be solved by the invention] However, with the conventional improvements mainly in the cutting method, even if the slit suitability has been improved to some extent, it has not solved the practical problem, especially in the base for magnetic recording. For applications such as film, where adhesion of foreign matter and dust and hairs on the film edges are not preferred, polyester films, which have poor slit suitability, have a fatal drawback.

本発明は、かかる問題点を改善し、スリット適正に優れ
たポリエステルフィルム提供することを目的とする。
The object of the present invention is to improve such problems and provide a polyester film with excellent slit suitability.

[問題点を解決するための手段] 本発明は、ポリエステルフィルムを、20−/−を越え
、100に9/r:Xl以下の高圧下で、二酸化炭素と
窒素との体積混合率が1/99〜9515である混合気
体と接触せしめることを特徴とするポリエステルフィル
ムの処理方法を特徴とするものである。
[Means for Solving the Problems] The present invention provides a polyester film with a volumetric mixing ratio of carbon dioxide and nitrogen of 1/2 to 100 to 9/r:Xl or less under high pressure. The present invention is characterized by a method for treating a polyester film, which is characterized by bringing the polyester film into contact with a mixed gas having a molecular weight of 99 to 9515.

本発明におけるポリエステルとは、ジカルボン酸とジオ
ールとより縮重合により得られるエステル結合を分子主
鎖に有する高分子化学物であり、代表的なポリエステル
としては、ポリエチレンテレフタレート、ポリブチレン
テレフタレート、ポリエチレンナフタレート、ポリエチ
レンα、β−ビス(2−クロルフェノキシ)エタン4.
4’ −ジカルボキシレートなど、およびそれらに他の
コモノマーを共重合させたものや、i−チル結合を主鎖
に有するものなど含むものである。本発明の場合、ホモ
ポリマーである方が本発明の効果が顕著になる場合が多
い。ざらに本発明のポリエステルは、二軸延伸・熱処理
されたちの特に結晶化度40%以上、面配向度0.03
以上のものが特に好ましいが、必要によっては一軸延伸
・熱処理されたものにも適用することが出来る。もちろ
ん、ポリエステルには、高分子としての公知の添加剤、
例えば安定剤、粘度調製剤、酸化防止剤、充填剤、すべ
り剤、帯電防止剤、ブロッキング防止剤などを含有させ
てもよい。また、該ポリエステルフィルムの表面に、新
たな機能を付与するために別のポリマーをラミネートし
たり、あるいはコロナ放電などの表面処理をしてもよい
ことはもちろんである。フィルム厚さは特に限定しない
が、500μm以下、好ましくは100μm以下のもの
が、本発明の効果は顕著である。処理されるポリエステ
ルフィルムの形態は、フィルム一枚であっても、重ね合
わさったものでもよく、本発明の場合、特にロール状に
巻取られたポリエステルフィルムが経済性、使いやすさ
、実用性の上で好ましい形状である。
The polyester in the present invention is a polymeric chemical having an ester bond in the main chain of the molecule obtained by condensation polymerization of a dicarboxylic acid and a diol. Typical polyesters include polyethylene terephthalate, polybutylene terephthalate, and polyethylene naphthalate. , polyethylene α,β-bis(2-chlorophenoxy)ethane4.
These include 4'-dicarboxylate, those copolymerized with other comonomers, and those having an i-thyl bond in the main chain. In the case of the present invention, the effects of the present invention are often more pronounced when the polymer is a homopolymer. Roughly, the polyester of the present invention is biaxially stretched and heat treated, and has a crystallinity of 40% or more and a plane orientation of 0.03.
Although the above-mentioned materials are particularly preferred, materials that have been uniaxially stretched and heat-treated can also be applied if necessary. Of course, polyester contains known additives as polymers,
For example, stabilizers, viscosity modifiers, antioxidants, fillers, slip agents, antistatic agents, antiblocking agents, and the like may be included. It goes without saying that the surface of the polyester film may be laminated with another polymer or subjected to surface treatment such as corona discharge in order to impart a new function. Although the film thickness is not particularly limited, the effect of the present invention is significant when the film thickness is 500 μm or less, preferably 100 μm or less. The polyester film to be processed may be in the form of a single film or a layered film, and in the case of the present invention, polyester film wound into a roll is particularly suitable for economic efficiency, ease of use, and practicality. This is the preferred shape.

次に、処理する混合気体は、二酸化炭素(C02)と窒
素(N2)との体積混合率が1/99〜9515、好ま
しくは、5/95〜80/20の範囲になければならな
い。CO2ガスが1%未満、好ましくは5%未満のとき
は、本発明の効果であるスリット適正の向上が達成でき
ないためである。
Next, the mixed gas to be treated must have a volumetric mixing ratio of carbon dioxide (C02) and nitrogen (N2) in the range of 1/99 to 9515, preferably 5/95 to 80/20. This is because when the CO2 gas content is less than 1%, preferably less than 5%, the improvement in slit suitability, which is an effect of the present invention, cannot be achieved.

一方、CO2ガスが95%を越えるとき、好ましくは8
0%を越えるときも、上記と同等にスリット適正の向上
が出来ないのである。以上のように、CO2とN2とが
、ある混合比率のときのみにポリエステルフィルムのス
リット適正を向上させることが出来るのである。すなわ
ち本発明の場合、窒素ガスの含有を必須要件とし、窒素
ガスが5%以上、好ましくは20%以上含有していない
と、特に結晶化度が40%以上もある二軸配向ポリエス
テルフィルムに対してはスリット適正の向上が期待でき
ないのである。
On the other hand, when CO2 gas exceeds 95%, preferably 8
Even when it exceeds 0%, the slit suitability cannot be improved to the same extent as above. As described above, it is possible to improve the slitting suitability of a polyester film only when CO2 and N2 are mixed at a certain mixing ratio. In other words, in the case of the present invention, the inclusion of nitrogen gas is an essential requirement, and if the nitrogen gas is not contained at 5% or more, preferably 20% or more, the biaxially oriented polyester film, which has a crystallinity of 40% or more, cannot be used. Therefore, no improvement in slit suitability can be expected.

もちろん、CO2とN2以外の気体が少量混在していて
も良く、例えば酸素、水蒸気、アルゴン、酸化窒素(N
o1NO2、N20、N2O3、N2O5、N03)、
酸化炭素(CoSC302、C502)ヘリウムなどで
あり、CO2とN2以外の気体は全体積中に、50%未
満、好ましくは30%未満であるのがよい。また水蒸気
を10〜45RH%と低く含有すると本発明の効果を顕
著にする。
Of course, a small amount of gas other than CO2 and N2 may be mixed, such as oxygen, water vapor, argon, nitrogen oxide (N
o1NO2, N20, N2O3, N2O5, N03),
Carbon oxide (CoSC302, C502), helium, etc., and gases other than CO2 and N2 should account for less than 50%, preferably less than 30%, of the total volume. Furthermore, when water vapor is contained as low as 10 to 45 RH%, the effect of the present invention becomes remarkable.

次に混合気体を20に9/cnfを越え、1001q/
d以下、好ましくは25〜50kcJ/cy+fに加圧
しなければならない。圧力が20に+1/cnf以下、
好ましくは25に9/−未満と低い時は、たとえ混合ガ
スの体積比が上記範囲内にあっても、本発明の目的であ
るポリエステルフィルムのスリット適正を向上させるこ
とが出来ないためである。逆に圧力が100に9/cn
fを越えるとき、好ましくは50kci/−を越える時
にも、上記と同じ様に本発明の効果が認められないのみ
ならず、ポリエステルフィルムが変形をうけて歪んでし
まうためである。すなわち本発明は、特定のガス組成と
、特定の4力範囲を満足する時にのみ、スリット性の向
上などの優れた効果が発揮するのである。
Next, the mixed gas is increased to 20 to exceed 9/cnf and 1001q/
The pressure must be d or less, preferably 25 to 50 kcJ/cy+f. Pressure is below 20+1/cnf,
This is because if it is low, preferably less than 25 to 9/-, even if the volume ratio of the mixed gas is within the above range, the slitting suitability of the polyester film, which is the object of the present invention, cannot be improved. Conversely, the pressure is 100 to 9/cn
This is because when it exceeds f, preferably when it exceeds 50 kci/-, not only the effect of the present invention is not recognized as described above, but also the polyester film is deformed and distorted. That is, the present invention exhibits excellent effects such as improved slitting performance only when a specific gas composition and a specific four force range are satisfied.

また、この時の処理温度は、該ポリエステルのガラス転
移温度■gより40℃高い温度で、かつ冷結晶化温度T
CC以下の温度から、Tgより40’C低い温度の範囲
が有効であるが、必ずしもこれに限定されない。しかし
Tg以下の処理の方が総合的効果は顕著である。
In addition, the treatment temperature at this time is 40°C higher than the glass transition temperature (g) of the polyester, and the cold crystallization temperature (T).
A range of temperatures from below CC to temperatures 40'C below Tg is effective, but is not necessarily limited thereto. However, the overall effect of treatment below Tg is more significant.

次に処理に必要な時間は、処理温度や目的によって異な
るが、スリット性の向上を目的とする場合は、4時間以
上、好ましくは20時間から75時間程度の処理がよい
The time required for the next treatment varies depending on the treatment temperature and purpose, but if the purpose is to improve slitting properties, treatment for 4 hours or more, preferably about 20 to 75 hours is recommended.

[物性の測定方法] (1)ガラス転移温度(T(J>は、サンプル5mgを
走査型熱量計(DSC>にセットし、20℃/分の昇温
速度で窒素気流下で加熱してゆき、ベースラインが偏奇
し始める温度ともとにもどる温度との相加平均値を用い
る。あるいは、サンプルによっては、吸熱ピークのよう
な形状となる時は、その頂上を採用する。
[Method for measuring physical properties] (1) Glass transition temperature (T (J)) is determined by setting 5 mg of the sample in a scanning calorimeter (DSC) and heating it under a nitrogen stream at a heating rate of 20°C/min. , the arithmetic mean value of the temperature at which the baseline begins to become eccentric and the temperature at which it returns to its original value is used.Alternatively, depending on the sample, if the shape resembles an endothermic peak, the peak thereof is used.

(2)  冷結晶化温度(TCC>は、上記Tgを求め
た時と同様にしてサーモグラフを書かせ、TIJの次に
出る結晶化にもとずく発熱のピーク温度を採用する。
(2) For the cold crystallization temperature (TCC>), draw a thermograph in the same manner as when determining Tg above, and use the peak temperature of exotherm based on crystallization that appears next to TIJ.

(3〉  スリット性の評価 厚さ14.5μmのPETフィルムの片面に下記組成の
磁性塗布液を、乾燥後膜厚が3μmとなるようにコーテ
ィングする。
(3> Evaluation of slitting properties One side of a PET film with a thickness of 14.5 μm is coated with a magnetic coating liquid having the following composition so that the film thickness after drying is 3 μm.

(重量部) ポリエステルポリウレタン樹脂   35塩ビ・マイレ
ン酸共重合体     30α−アルミナ      
      15カーボンブラツク         
 3オレイン酸              5アミル
ステアレート          4トリイソシアネ一
ト化合物     22強磁性金属粉末       
  300酢酸ブチル           300メ
チルイソブチルケトン     300コーテイング後
、直流磁場中で配向し、乾燥した後、カレンダー加工を
施す。このシートをシェアカッターで1/2インチ幅に
スリットしてビデオテープとする。このシェアカッター
によるスリット箇所を目視観察して、ヒゲや粉の発生具
合の程度を次の5等級に分けて評価する。
(Parts by weight) Polyester polyurethane resin 35 PVC/maleic acid copolymer 30 α-alumina
15 carbon black
3 Oleic acid 5 Amyl stearate 4 Triisocyanate compound 22 Ferromagnetic metal powder
300 Butyl acetate 300 Methyl isobutyl ketone 300 After coating, it is oriented in a DC magnetic field, dried, and then calendered. This sheet is slit into 1/2 inch width using a shear cutter to make a videotape. The slit location made by this shear cutter is visually observed, and the degree of generation of whiskers and powder is evaluated by dividing it into the following five grades.

スリット性A:ヒゲや粉の発生が非常に少ない。Slitting property A: There is very little generation of whiskers and powder.

tr   3 :    v     少ない。tr 3: v Few.

〃  C:   〃    普通レベル。C: Normal level.

+7   D :    v     ヤや多い。+7 D: There are many V -ya.

〃  E:   〃    多い。E: A lot.

(注)、なお、現在市販されているビデオテープ用二軸
配向PETフィルムのスリット性のレベルは、Cまたは
Dのものが多い。
(Note) Most of the biaxially oriented PET films for video tapes currently on the market have a slitting level of C or D.

(4)面配向係数 フィルムを約50μmの厚さに積層してX線回折用試料
とし、X線回折装置(理学電気(株)製Ge i ge
rf l ex)の試料ホルダーに設置する。
(4) Planar orientation coefficient films were laminated to a thickness of approximately 50 μm to prepare a sample for X-ray diffraction, and an X-ray diffraction apparatus (Ge ige manufactured by Rigaku Denki Co., Ltd.
rf l ex) sample holder.

フィルムの長手方向に垂直な面内で、X線の照射角を変
え、反射法で回折強度を測定する。測定条件は次の通り
である。
The diffraction intensity is measured using a reflection method by changing the irradiation angle of X-rays in a plane perpendicular to the longitudinal direction of the film. The measurement conditions are as follows.

時定数        = 2秒 走引速度       : 1度/分 o;vergency s+;t    :  1.5
mmΦScattetringSIit   :  1
度Receiving 5lit      :  Q
、3mmX線  :Cu対陰極によるCu−にα線(3
5KV115mA、 Ni−フィルター)PET結晶の
[100]、[ITO]面の回折角に相当する26.0
’ 、22.5°での回折強度をそれぞれI1、I2と
すると、面配向係数はそれらの比(II/I2)で与え
られる。
Time constant = 2 seconds Traveling speed: 1 degree/min o; vergency s+; t: 1.5
mmΦScattetringSIit: 1
Degree Receiving 5lit: Q
, 3mm X-ray: α rays (3mm
5KV115mA, Ni-filter) 26.0, which corresponds to the diffraction angle of the [100] and [ITO] planes of the PET crystal.
When the diffraction intensities at ' and 22.5 degrees are respectively I1 and I2, the plane orientation coefficient is given by their ratio (II/I2).

[実施例] 本発明を実施例にもとすいて説明する。[Example] The present invention will be explained based on examples.

実施例1〜9 比較例1〜5 ポリエチレンテレフタレート(O−クロルフェノール中
での極限粘度0.61、添加剤として平均径150μm
の酸化チタンを0.15%および平均粒径800mμの
合成炭酸カルシウム0.06%含有)を常法により28
5℃で溶融させ、Tダオロ金から吐出させ、静電荷を印
加させなから25°Cに保たれたキャスティングドラム
で成形した。次に該キャストフィルムを、95℃に加熱
された縦延伸ロール上で3.7倍延伸したのち、テンタ
ー内で90℃で4.2倍横延伸し、続いて190℃で3
秒間巾方向に5%リラックスさせながら熱処理後、ざら
に130℃で5秒間定長熱処理した。かくして得られた
厚さ75μmのフィルムを中間スプールとして−Hロー
ル状に巻取ったのちに、両耳をスリットして製品ロール
とした。
Examples 1 to 9 Comparative Examples 1 to 5 Polyethylene terephthalate (intrinsic viscosity in O-chlorophenol 0.61, average diameter 150 μm as an additive)
(containing 0.15% titanium oxide and 0.06% synthetic calcium carbonate with an average particle size of 800 mμ) by a conventional method.
It was melted at 5°C, discharged from a T dauro gold, and molded in a casting drum maintained at 25°C without applying an electrostatic charge. Next, the cast film was stretched 3.7 times on a longitudinal stretching roll heated to 95°C, then horizontally stretched 4.2 times at 90°C in a tenter, and then 3x stretched at 190°C.
After heat treatment while relaxing 5% in the width direction for seconds, it was roughly heat treated at 130° C. for 5 seconds at a fixed length. The thus obtained film having a thickness of 75 μm was wound up into a -H roll as an intermediate spool, and then both ends were slit to obtain a product roll.

かくして得られたロール状に巻取られた二軸配向ポリエ
チレンテレフタレートを表1に示すようなCO2/N2
混合ガス下で、加圧しながら45℃の雰囲気温度で24
時間処理をした。
The biaxially oriented polyethylene terephthalate thus obtained was wound up into a roll with CO2/N2 as shown in Table 1.
24 hours at an ambient temperature of 45°C under pressure under mixed gas.
I processed the time.

表1 [発明の効果] 本発明は、ポリエステルフィルムを二酸化炭素と窒素の
混合ガス中でしかも加圧下で処理をしたので、次のよう
な優れた効果を奏するものである。
Table 1 [Effects of the Invention] In the present invention, a polyester film is treated in a mixed gas of carbon dioxide and nitrogen under pressure, and therefore, the following excellent effects are achieved.

(1)  スリット性に優れたフィルムが得られる。(1) A film with excellent slitting properties can be obtained.

(2)  ざらに、易接着性、易滑性にも優れたフィル
ムとなる。
(2) The resulting film has excellent roughness, easy adhesion, and easy sliding properties.

(3〉  また、オリゴマーなどの低分子最のブリード
アウト防止にも効果がある。
(3) It is also effective in preventing bleed-out of low molecules such as oligomers.

(4)  さらに、酸素、水蒸気などのガスバリア性に
も優れたフィルムとなる。
(4) Furthermore, the film has excellent barrier properties against gases such as oxygen and water vapor.

かくして得られる本発明のポリエステルフィルムは、ス
リット適正に優れ、しかも、易接着性にも優れているた
めに、磁気記録、光記録などの記録用ベースフィルムな
どに用いられ、優れた性能を発揮する。もちろん、本発
明で得られたポリエステルフィルムは、スリット適正の
必ずしも必要としない用途にも利用できることは明らか
である。
The thus obtained polyester film of the present invention has excellent slit suitability and easy adhesion, so it can be used as a base film for recording such as magnetic recording and optical recording, and exhibits excellent performance. . Of course, it is clear that the polyester film obtained by the present invention can also be used for applications that do not necessarily require proper slitting.

Claims (1)

【特許請求の範囲】[Claims] ポリエステルフィルムを、20kg/cm^2を越え、
100kg/cm^2以下の高圧下で、二酸化炭素と窒
素との体積混合率が1/99〜95/5である混合気体
と接触せしめることを特徴とするポリエステルフィルム
の処理方法。
polyester film over 20kg/cm^2,
A method for treating a polyester film, which comprises bringing it into contact with a mixed gas of carbon dioxide and nitrogen having a volumetric mixing ratio of 1/99 to 95/5 under high pressure of 100 kg/cm^2 or less.
JP30869086A 1986-12-26 1986-12-26 Treating process of polyester film Pending JPS63162223A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30869086A JPS63162223A (en) 1986-12-26 1986-12-26 Treating process of polyester film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30869086A JPS63162223A (en) 1986-12-26 1986-12-26 Treating process of polyester film

Publications (1)

Publication Number Publication Date
JPS63162223A true JPS63162223A (en) 1988-07-05

Family

ID=17984108

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30869086A Pending JPS63162223A (en) 1986-12-26 1986-12-26 Treating process of polyester film

Country Status (1)

Country Link
JP (1) JPS63162223A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU631339B2 (en) * 1990-02-20 1992-11-19 E.I. Du Pont De Nemours And Company Thermoformable composite sheet
WO2001094102A1 (en) * 2000-06-07 2001-12-13 Sig Simonazzi S.P.A. A material with a high degree of impermeability to gases and a method for the production thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU631339B2 (en) * 1990-02-20 1992-11-19 E.I. Du Pont De Nemours And Company Thermoformable composite sheet
WO2001094102A1 (en) * 2000-06-07 2001-12-13 Sig Simonazzi S.P.A. A material with a high degree of impermeability to gases and a method for the production thereof

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