JPH02235615A - Manufacture of polyester film - Google Patents
Manufacture of polyester filmInfo
- Publication number
- JPH02235615A JPH02235615A JP1058243A JP5824389A JPH02235615A JP H02235615 A JPH02235615 A JP H02235615A JP 1058243 A JP1058243 A JP 1058243A JP 5824389 A JP5824389 A JP 5824389A JP H02235615 A JPH02235615 A JP H02235615A
- Authority
- JP
- Japan
- Prior art keywords
- film
- stretching
- water
- liquid film
- longitudinal direction
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 229920006267 polyester film Polymers 0.000 title claims description 5
- 238000001816 cooling Methods 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 229920000728 polyester Polymers 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 abstract description 35
- 238000005266 casting Methods 0.000 abstract description 8
- 238000005507 spraying Methods 0.000 abstract description 2
- 238000007711 solidification Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- 230000005499 meniscus Effects 0.000 description 5
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- -1 polyethylene terephthalate Polymers 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 description 3
- 239000005020 polyethylene terephthalate Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 230000003746 surface roughness Effects 0.000 description 3
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 3
- SVTBMSDMJJWYQN-UHFFFAOYSA-N 2-methylpentane-2,4-diol Chemical compound CC(O)CC(C)(C)O SVTBMSDMJJWYQN-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010292 electrical insulation Methods 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- BXGYYDRIMBPOMN-UHFFFAOYSA-N 2-(hydroxymethoxy)ethoxymethanol Chemical compound OCOCCOCO BXGYYDRIMBPOMN-UHFFFAOYSA-N 0.000 description 1
- WMRCTEPOPAZMMN-UHFFFAOYSA-N 2-undecylpropanedioic acid Chemical compound CCCCCCCCCCCC(C(O)=O)C(O)=O WMRCTEPOPAZMMN-UHFFFAOYSA-N 0.000 description 1
- WSQZNZLOZXSBHA-UHFFFAOYSA-N 3,8-dioxabicyclo[8.2.2]tetradeca-1(12),10,13-triene-2,9-dione Chemical compound O=C1OCCCCOC(=O)C2=CC=C1C=C2 WSQZNZLOZXSBHA-UHFFFAOYSA-N 0.000 description 1
- GXGJIOMUZAGVEH-UHFFFAOYSA-N Chamazulene Chemical group CCC1=CC=C(C)C2=CC=C(C)C2=C1 GXGJIOMUZAGVEH-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- QYQADNCHXSEGJT-UHFFFAOYSA-N cyclohexane-1,1-dicarboxylate;hydron Chemical compound OC(=O)C1(C(O)=O)CCCCC1 QYQADNCHXSEGJT-UHFFFAOYSA-N 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229940051250 hexylene glycol Drugs 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000001465 metallisation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920003207 poly(ethylene-2,6-naphthalate) Polymers 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 239000011112 polyethylene naphthalate Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 239000012748 slip agent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000004034 viscosity adjusting agent Substances 0.000 description 1
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
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製造方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a polyester film.
[従来の技術]
ポリエステルシートに水などの液膜を介在させた冷却体
表面上でキャストする方法は、B P 1140175
、特公昭5g−35133号公報などで知られている。[Prior Art] A method of casting a polyester sheet on the surface of a cooling body with a liquid film such as water interposed therein is described in BP 1140175.
, is known from Japanese Patent Publication No. 5G-35133.
また、ポリエステルの長手方向の延伸を、2段階以上の
多段階で高倍率延伸することは、特公昭52−1090
9号公報、特公昭52−33666号公報などで公知で
ある。In addition, the stretching of polyester in the longitudinal direction at a high magnification in two or more stages is disclosed in Japanese Patent Publication No. 52-1090.
This method is known from Japanese Patent Publication No. 9, Japanese Patent Publication No. 52-33666, and the like.
[発明が解決しようとする課題]
しかし、上記それぞれの製造方法では次のような欠点を
有している。[Problems to be Solved by the Invention] However, each of the above manufacturing methods has the following drawbacks.
(1)長手方向の延伸倍率を高くとるために、延伸温度
を高くし、多段階に分けて延伸される(高温高倍率延伸
)。このために、得られたフィルムの厚みむらが大きく
なり、さらに表面が荒れたり、表面が摩耗しやすくなっ
たりする。(1) In order to obtain a high stretching ratio in the longitudinal direction, the stretching temperature is increased and the stretching is performed in multiple stages (high-temperature high-magnification stretching). For this reason, the thickness of the obtained film increases, and the surface becomes rough and easily abraded.
■ 高温高倍率で延伸するため、延伸ロールが汚れやす
く、得られたフィルムの表面欠点を誘発しやすくなり、
ロールの清浄や交換などで生産性を阻害する。■ Because stretching is carried out at high temperature and high magnification, the stretching rolls are easily soiled and the resulting film is more likely to develop surface defects.
Productivity is hindered by cleaning and replacing rolls.
(3)液膜を介在させると、冷却体表面上で溶融シート
がすべりやすい。(3) When a liquid film is present, the molten sheet easily slides on the surface of the cooling body.
[課題を解決するための手段]
本発明は、上記欠点を改善した高倍率延伸方法を提供す
ることを目的としている。すなわち、溶融ポリエステル
シー1・を、水の液膜を有した冷却体表面上で密着冷却
固化させたのちに、長手方向に多段階で総合延伸倍率4
.5倍以上延伸することを特徴とするボリエ.ステルフ
ィルムの製造方法に関するものである。[Means for Solving the Problems] An object of the present invention is to provide a high-magnification stretching method that improves the above-mentioned drawbacks. That is, after the molten polyester sheet 1 is tightly cooled and solidified on the surface of the cooling body having a liquid film of water, the total stretching ratio is 4 in multiple steps in the longitudinal direction.
.. Bolier characterized by being stretched 5 times or more. The present invention relates to a method for producing stell film.
本発明のポリエステルとは、グライコールとジカルボン
酸の縮重合によって得られる主鎖にエステル結合を有す
るボリマーの総称であり、代表的なグライコールとして
は、エチレングリコール、ブタンジオール、ヘキシレン
グリコール、シクロヘキサンジメタノール、ネオペンチ
ルグリコール、などで、代表的なジカルボン酸としては
、テレフタル酸、イソフタル酸、フタル酸、ナフタレン
ジカルボン酸、ジフェニルジカルボン酸、シクロヘキサ
ンジカルボン酸、アジピン酸、セバチン酸、ドデカンジ
カルボン酸、ダイマー酸、エイコ酸などである。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
、ボチブチレンテレフタレート、ポリエチレンナフタレ
ート、ボリシクロヘキシレンジメチレンテ12ノフタレ
ート、などであり、特に本発明の場合、ポリエチレンテ
レフタ1、・−トが好ましい。The polyester of the present invention is a general term for polymers having ester bonds in the main chain obtained by condensation polymerization of glycol and dicarboxylic acid. Typical glycols include ethylene glycol, butanediol, hexylene glycol, and cyclohexane. Dimethanol, neopentyl glycol, etc. Typical dicarboxylic acids include terephthalic acid, isophthalic acid, phthalic acid, naphthalenedicarboxylic acid, diphenyldicarboxylic acid, cyclohexanedicarboxylic acid, adipic acid, sebacic acid, dodecanedicarboxylic acid, dimer acids, eicoic acids, etc. Typical polyesters include polyethylene terephthalate, butylene terephthalate, polyethylene naphthalate, polycyclohexylene dimethylene 12 nophthalate, etc., and particularly preferred in the present invention are polyethylene terephthalate 1, -.
もちろん、上記ポリマーに公知の添加剤、例えば安定剤
、粘度調整剤、酸化防止剤、充填剤、滑り剤、帯電防止
剤、プロツキング防止剤、離型剤などを含有させてもよ
い。Of course, the above polymer may contain known additives such as stabilizers, viscosity modifiers, antioxidants, fillers, slip agents, antistatic agents, antiblocking agents, mold release agents, and the like.
冷却体表面」二に液膜を介在させる方法としては、湿気
を含んだ空気を、その露点以下に保たれた冷却体表面に
吹きつけて結露させる方法(結露法)や、しみ出しロー
ラーあるいは転写ローラーで塗布する方法、静電荷を帯
びた水蒸気を噴霧する方法などがあるが、水の液膜の平
均膜厚さdが3μm以下と薄い方が優れている本発明の
場合には、結露法が好ましい。この水の液の平均膜厚さ
dは、赤外線吸収法より水の重量から換算して求める。Methods for interposing a liquid film on the surface of the cooling body include a method of blowing humid air onto the surface of the cooling body kept below its dew point to cause condensation (condensation method), and a method using a seepage roller or transfer method. There are methods such as coating with a roller and spraying water vapor with an electrostatic charge, but in the case of the present invention, where the thinner average film thickness d of the water film is 3 μm or less, the better, the condensation method is used. is preferred. The average film thickness d of this water liquid is calculated from the weight of water using an infrared absorption method.
測定は、直接冷却体表面」二にある液膜の厚さを求める
。また必要なら、溶融シート上から冷却体表面上に向か
って溶融シートと冷却体表面間に介在する液膜の厚さも
測定することができる。なお、液膜という表現をとって
いるが、必ず1,も液体が均一な連続膜になっている必
要はなく、結露法で得られるような不連続の液滴の集合
であってもよい。The measurement directly determines the thickness of the liquid film on the surface of the cooling body. If necessary, it is also possible to measure the thickness of the liquid film interposed between the molten sheet and the surface of the cooling body from the top of the molten sheet onto the surface of the cooling body. Although the expression "liquid film" is used, the liquid does not necessarily have to form a uniform continuous film, and may be a collection of discontinuous droplets such as those obtained by a dew condensation method.
また、溶融シートと冷却体表面との接する位置に形成さ
れるメニスカスの高さhは、上記水の液膜の平均膜厚さ
dよりも大きいことが好ましい。Further, it is preferable that the height h of the meniscus formed at the position where the molten sheet contacts the surface of the cooling body is larger than the average film thickness d of the water film.
このメニスカスの高さhは、種々の要因で変わり、ポリ
マーの表面張力、溶融シート表面粗さ、冷却体表面の粗
さや表面張力、静電印加法などの他の密着手段による補
助密着力、吐出する口金から冷却体表面までの距離、溶
融シートのドラムへの密着する角度、冷却体表面にある
液滴の存在密度と液滴の大きさなどに依存する。すなわ
ち、これらのパラメーターを適宜組み合わせることによ
りメニスカスの高さhを変えることができる。メニスカ
スの高さは、溶融体と冷却体表面との接点近傍に出来る
液の表面張力に起因する三日月形の冷却体表面から垂直
方向の高さをいう。hの測定には精度がいるために、フ
ァイバースコープなどで写真に撮ったのちに解析して求
めるのがよい。hの値としては1〜20μmSdの値と
して3μIn以下0. 1μm以上であり、しかもh
>d,好ましくはh>2dを満足するようなときに安定
したキャストシ一トが得られるので好ましい。The height h of this meniscus varies depending on various factors, such as the surface tension of the polymer, the surface roughness of the molten sheet, the roughness and surface tension of the cooling body surface, the auxiliary adhesion force by other adhesion methods such as electrostatic application, and the discharge It depends on the distance from the die to the surface of the cooling body, the angle at which the molten sheet comes into close contact with the drum, the density of droplets on the surface of the cooling body, the size of the droplets, etc. That is, the height h of the meniscus can be changed by appropriately combining these parameters. The height of the meniscus refers to the height in the vertical direction from the crescent-shaped cooling body surface, which is caused by the surface tension of the liquid created near the contact point between the molten body and the cooling body surface. Measuring h requires precision, so it is best to take a photo with a fiberscope and then analyze it. The value of h is 1 to 20 μmSd and is 3 μIn or less and 0. 1 μm or more, and h
>d, preferably h>2d, since a stable cast sheet can be obtained.
なお、静電荷を印加させながらキャストする方法として
、特公昭37−6142などで公知の方法を併用するこ
とができる。In addition, as a method of casting while applying an electrostatic charge, a method known in Japanese Patent Publication No. 37-6142 and the like can be used in combination.
長手方向に高倍率に延伸する方法として特公昭52−3
3666号公報などで公知のように、高温で延伸する工
程と、低温で延伸する工程とからなる多段階延伸方式が
知られている。このように多段階で延伸することにより
長手力向の延伸倍率は特公昭38−23489号公報な
どで知られているような2.5〜3.5倍の約2倍の5
〜9倍程度に高くとれるため、200m/分以上の高速
度製膜が可能になる。確かに多段階延伸法はコストダウ
ンプロセスには好まし7い方法であるが、得られたフィ
ルムは厚みむらが大きくフィルム表面が荒れたり、さら
には耐摩耗性の弱いフィルム表面となったりして品質上
の問題があるのみならず、延伸ロールが短時間に汚れや
すいために、フイルム表面欠点となるなどの問題点を有
していた。すなわち、長手方向の総合延伸倍率を4.5
倍以上と高くすると、品質上、生産上の問題が生じてく
るという致命的な欠点を有していた。As a method of stretching at a high magnification in the longitudinal direction,
As is known from Japanese Patent Application No. 3666, a multi-stage stretching method is known which includes a step of stretching at a high temperature and a step of stretching at a low temperature. By stretching in multiple stages in this way, the stretching ratio in the longitudinal direction can be increased to 5.
Since the speed can be approximately 9 times higher, high-speed film formation of 200 m/min or more is possible. It is true that the multi-step stretching method is a preferable method for cost reduction processes, but the resulting film has large thickness irregularities, a rough film surface, and even a film surface with poor abrasion resistance. Not only are there problems in terms of quality, but the stretching rolls tend to become dirty in a short period of time, resulting in defects on the film surface. In other words, the total stretching ratio in the longitudinal direction is 4.5.
If it were made to be more than twice as high, it would have the fatal disadvantage of causing problems in terms of quality and production.
ところが、このような総合延伸倍率4.5倍以上延伸す
るキャストシ一トを、特定の条件で製膜したものにすれ
ば、上記のような欠点が発生しないことを見い出し本発
明に到ったものである。すなわち、キャストシ一トとし
ては、水の液膜を有した冷却体表面上で密着冷却固化さ
せたポリエステルシートを用いれば上記欠点は解消でき
る。このとき、キャスト時に静電荷を印加させながら冷
却固化させれば、さらにその効果は大きくなる。However, it was discovered that if such a cast sheet, which is stretched at a total stretching ratio of 4.5 times or more, is formed into a film under specific conditions, the above-mentioned drawbacks will not occur, resulting in the present invention. It is. That is, the above-mentioned drawbacks can be overcome by using a polyester sheet that is cooled and solidified in close contact with the surface of a cooling body having a liquid film of water as the cast sheet. At this time, the effect will be even greater if the material is cooled and solidified while applying an electrostatic charge during casting.
長手方向の延伸方法としては、降伏点以下で多段階に延
伸したのち、ほぼ通常の延伸を行なう方法や、高温低延
伸速度で約2倍延伸後、ほぼ通常の延伸を2.5〜3,
5倍延伸し、トータル4.5〜7倍に延伸する方法など
があるが、いずれも通常の長手力向の延伸温度に比べて
高温で延伸する必要がある。延伸倍率として4.5倍以
上、好ましくは5倍〜9倍の延伸倍率のものに本発明の
効果は顕著である。延伸速度は高温延伸するときには、
出来る限りゆっくりした速度、たとえば10000%/
分以下で行なうのが好ましいが、これに限定されるもの
ではない。The stretching method in the longitudinal direction includes multi-stage stretching below the yield point, followed by almost normal stretching, and a method of stretching approximately 2 times at a high temperature and low stretching speed, followed by approximately normal stretching 2.5 to 3 times.
There are methods of stretching 5 times and stretching 4.5 to 7 times in total, but all of them require stretching at a higher temperature than the normal stretching temperature in the longitudinal direction. The effect of the present invention is remarkable when the stretching ratio is 4.5 times or more, preferably 5 times to 9 times. When stretching at high temperature, the stretching speed is
As slow a speed as possible, for example 10000%/
It is preferable to carry out the reaction in minutes or less, but the time is not limited thereto.
かくして得られた長手方向延伸フイルムを、必要に応じ
て巾方向に延伸したり、熱処理をしてもよいことは明ら
かである。特に本発明の場合、二軸延伸することにより
その効果は顕著になるのである。It is clear that the longitudinally stretched film thus obtained may be stretched in the width direction or heat treated as required. Particularly in the case of the present invention, the effect becomes remarkable by biaxial stretching.
[測定法] 本発明で使用した語句の測定法を述べる。[Measurement method] A method for measuring words used in the present invention will be described.
(1)厚みむら
所定の方向にフィルムサンプルを長手方向には10m長
、幅方向には最大長のサンプリングし、それを歪ゲージ
で連続的に厚みを測定し、最大厚さと最小厚さとの厚み
差Δdを平均厚みdで割った値を百分率で示したもの。(1) Thickness unevenness Sample a film sample in a predetermined direction with a length of 10 m in the longitudinal direction and the maximum length in the width direction, measure the thickness continuously with a strain gauge, and calculate the thickness between the maximum thickness and the minimum thickness. The value obtained by dividing the difference Δd by the average thickness d, expressed as a percentage.
2 表面粗さR,
JIS−80601−1976に従いカットオフ0、2
5mmで測定した最大粗さR.である。2 Surface roughness R, cutoff 0, 2 according to JIS-80601-1976
Maximum roughness measured at 5mm R. It is.
(3)外部ヘイズ
JIS−K6714に従い測定したトータルヘイズから
、テトラリン液中にて測定した内部ヘイズを引いた値を
外部ヘイズとする。(3) External Haze The value obtained by subtracting the internal haze measured in the tetralin solution from the total haze measured according to JIS-K6714 is defined as the external haze.
[発明の効果]
高温高倍率延伸するのに、特定のキャスト法を用いたシ
ートを使うことにより、次のような効果が生じる。[Effects of the Invention] The following effects are produced by using a sheet using a specific casting method for high-temperature, high-magnification stretching.
(1) 長手方向の延伸倍率が4.5倍以上と高いに
もかかわらず厚みむらの小さい、表面の平滑なフィルム
が得られる。(1) Even though the stretching ratio in the longitudinal direction is as high as 4.5 times or more, a film with small thickness unevenness and a smooth surface can be obtained.
■ 得られたフィルムは、耐摩耗性にすぐれており、.
さらに長手方向の強度も高く、磁気テープ用ベースフィ
ルムに好適な特性を有したフィルムとなる。■ The obtained film has excellent abrasion resistance.
Furthermore, the film has high strength in the longitudinal direction and has properties suitable for a base film for magnetic tape.
(3)オリゴマーや添加物がフィルム表面にブリードし
にくい安定したフィルムになり、電気絶縁用フィルムな
どの用途にすぐれたフィルムになる。(3) It becomes a stable film in which oligomers and additives do not easily bleed onto the film surface, making it excellent for applications such as electrical insulation films.
(4) コンデンサー用フィルムとして電気絶縁特性
のすぐれたフィルムが得られる。(4) A film with excellent electrical insulation properties can be obtained as a capacitor film.
(5)印刷性、金属蒸着性などの易接着性にすぐれたフ
ィルムが得られる。(5) A film with excellent adhesion properties such as printability and metal deposition properties can be obtained.
(6)延伸ロールが汚れにくく、ロールの洗浄や交換の
少ない延伸プロセスであり、生産性にすぐれたプロセス
である。(6) It is a stretching process in which the stretching rolls are less likely to get dirty, requiring less cleaning and replacement of the rolls, and is a highly productive process.
■ 通常キャストフィ゜ルムより低温延伸で同一配向を
得ることができ、破れの少ない安定した延伸が可能にな
る。■ The same orientation can be obtained by stretching at a lower temperature than with ordinary cast films, and stable stretching with less tearing is possible.
[実施例]
次に本発明の効果をより理解しやすくするために実施例
で説明する。[Example] Next, in order to make it easier to understand the effects of the present invention, an example will be described.
実施例1
ポリエチレンテレフタレート(0−クロロフェノール中
での極限粘度[η]0.65、添加剤として平均粒径3
00mμのT i 02を0. 1重量%添加)を用
い、常法により180℃で真空乾燥後、押出機に供給し
、285℃で溶融させたのち、ギャーポンプで定量的に
計量し、Tダイ口金から一定厚さの溶融シートを吐出さ
せた。該シートの全中にわたって静電荷を印加させなが
ら50m/分で鏡面ドラム(表面粗さR.0.1μm)
上に密着冷却固化させた。このとき鏡面ドラム上には、
80℃の飽和水蒸気を含んだエアーを、25℃に保たれ
たドラムに吹き付け、平均水膜厚さdが1μmになる様
に均一に水の液滴が付着させてある。Example 1 Polyethylene terephthalate (intrinsic viscosity [η] in 0-chlorophenol 0.65, average particle size 3 as an additive)
T i 02 of 00 mμ is 0. After drying under vacuum at 180°C using a conventional method, the mixture was fed to an extruder, melted at 285°C, quantitatively measured using a gear pump, and melted to a constant thickness from a T-die nozzle. The sheet was discharged. A mirror-finished drum (surface roughness R. 0.1 μm) at 50 m/min while applying an electrostatic charge throughout the sheet.
It was cooled and solidified in close contact with the top. At this time, on the mirror drum,
Air containing saturated water vapor at 80° C. is blown onto a drum maintained at 25° C., and water droplets are uniformly deposited on the drum so that the average water film thickness d is 1 μm.
また、静電荷を帯びた溶融シートと冷却ドラムとの間に
出来る水のメニスカス高さhを2.5μmに保った。In addition, the height h of the water meniscus formed between the electrostatically charged molten sheet and the cooling drum was maintained at 2.5 μm.
かくして得られたキャストフィルムを、100℃に加熱
されたロール上で長手力向に1.8倍延伸後、90℃に
加熱されたロール上で3.6倍延伸し長手方向にトータ
ル6.5倍延伸した。つづいて、95℃に加熱されたテ
ンター内で巾方向に4倍延伸し、210℃で7秒間、巾
方向に5%のリラックスをしながら熱処理をして厚さ1
2μmの二軸延伸ポリエステルフィルムを得た。The cast film thus obtained was stretched 1.8 times in the longitudinal direction on rolls heated to 100°C, and then stretched 3.6 times on rolls heated to 90°C to give a total length of 6.5 times in the longitudinal direction. Stretched twice. Next, it was stretched 4 times in the width direction in a tenter heated to 95°C, and heat treated at 210°C for 7 seconds while relaxing 5% in the width direction to a thickness of 1.
A 2 μm biaxially stretched polyester film was obtained.
長手力向延伸温度は比較的低温で高倍率延伸が可能であ
り、また長時間延伸してもロール上に付着物などの汚れ
はなく、安定した延伸が可能であった。かくして得られ
たフィルムの特性を表1に示す。The stretching temperature in the longitudinal direction was relatively low, allowing for high-magnification stretching, and stable stretching was possible with no deposits or other stains on the rolls even after prolonged stretching. Table 1 shows the properties of the film thus obtained.
上記特性を有するフィルムを磁気テープ用のべ一スフィ
ルムに使ったとき、走行性、すべり性にすぐれており、
しかも耐摩耗性にすぐれた磁気テープが得られる。When a film with the above characteristics is used as a base film for magnetic tape, it has excellent running and slipping properties.
Furthermore, a magnetic tape with excellent wear resistance can be obtained.
比較例1
実施例1で用いた水膜を介在させたキャスト法を、水膜
を介在させない通常の静電印加キャスト法に変えて、他
は、実施例1と全く同一にして二軸延伸熱処理した。Comparative Example 1 The casting method with a water film intervening used in Example 1 was changed to the normal electrostatic application casting method without intervening a water film, and the other conditions were completely the same as in Example 1, and biaxial stretching heat treatment was performed. did.
その結果、長手方向の延伸時に強く配向するためか、巾
方向の延伸でフィルム破れが多発して、安定な延伸がで
きなかったが、二軸延伸フィルムの品質を測定した結果
を表2に示した。As a result, due to strong orientation during stretching in the longitudinal direction, the film frequently broke during stretching in the width direction, making stable stretching impossible. However, the results of measuring the quality of the biaxially stretched film are shown in Table 2. Ta.
表1
このようにキャスト方法を特定しないと安定した延伸が
できないのみならず、優れた品質のフィルムが得られな
い。Table 1 As described above, unless the casting method is specified, not only stable stretching cannot be performed, but also a film of excellent quality cannot be obtained.
Claims (2)
却体表面上で密着冷却固化させたのちに、長手方向に多
段階で総合延伸倍率4.5倍以上延伸することを特徴と
するポリエステルフィルムの製造方法。(1) A polyester characterized in that a molten polyester sheet is cooled and solidified in close contact on the surface of a cooling body having a liquid film of water, and then stretched in multiple steps in the longitudinal direction at a total stretching ratio of 4.5 times or more. Film manufacturing method.
固化させることを特徴とする請求項(1)に記載のポリ
エステルフィルムの製造方法。(2) The method for producing a polyester film according to claim (1), wherein the polyester film is cooled and solidified in close contact with the surface of the cooling body while applying an electrostatic charge.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1058243A JPH069860B2 (en) | 1989-03-09 | 1989-03-09 | Method for producing polyester film |
DE68925429T DE68925429T3 (en) | 1988-06-23 | 1989-06-23 | METHOD FOR PRODUCING A POLYESTER FILM |
US07/455,399 US5076976A (en) | 1988-06-23 | 1989-06-23 | Process for producing polyester film |
EP89907298A EP0466921B2 (en) | 1988-06-23 | 1989-06-23 | Process for producing polyester film |
PCT/JP1989/000625 WO1989012544A1 (en) | 1988-06-23 | 1989-06-23 | Process for producing polyester film |
KR1019890701853A KR960007293B1 (en) | 1988-06-23 | 1989-06-23 | Process for producing polyester film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1058243A JPH069860B2 (en) | 1989-03-09 | 1989-03-09 | Method for producing polyester film |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02235615A true JPH02235615A (en) | 1990-09-18 |
JPH069860B2 JPH069860B2 (en) | 1994-02-09 |
Family
ID=13078677
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1058243A Expired - Fee Related JPH069860B2 (en) | 1988-06-23 | 1989-03-09 | Method for producing polyester film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH069860B2 (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5698138A (en) * | 1980-01-10 | 1981-08-07 | Teijin Ltd | Manufacture of thermoplastic copolimerized sheet |
JPS5863415A (en) * | 1981-10-13 | 1983-04-15 | Teijin Ltd | Quenching device for melted polymer sheet |
-
1989
- 1989-03-09 JP JP1058243A patent/JPH069860B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5698138A (en) * | 1980-01-10 | 1981-08-07 | Teijin Ltd | Manufacture of thermoplastic copolimerized sheet |
JPS5863415A (en) * | 1981-10-13 | 1983-04-15 | Teijin Ltd | Quenching device for melted polymer sheet |
Also Published As
Publication number | Publication date |
---|---|
JPH069860B2 (en) | 1994-02-09 |
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