JPH02305827A - Fabricable polyester film - Google Patents
Fabricable polyester filmInfo
- Publication number
- JPH02305827A JPH02305827A JP12673089A JP12673089A JPH02305827A JP H02305827 A JPH02305827 A JP H02305827A JP 12673089 A JP12673089 A JP 12673089A JP 12673089 A JP12673089 A JP 12673089A JP H02305827 A JPH02305827 A JP H02305827A
- Authority
- JP
- Japan
- Prior art keywords
- film
- lubricant
- copolymerized
- melting point
- particle size
- 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
- 229920006267 polyester film Polymers 0.000 title claims description 8
- 239000000314 lubricant Substances 0.000 claims abstract description 17
- 239000002245 particle Substances 0.000 claims abstract description 15
- 238000002844 melting Methods 0.000 claims abstract description 13
- 230000008018 melting Effects 0.000 claims abstract description 13
- 238000000465 moulding Methods 0.000 claims description 7
- 229920000728 polyester Polymers 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 10
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 abstract description 6
- 229920001634 Copolyester Polymers 0.000 abstract description 5
- 239000000377 silicon dioxide Substances 0.000 abstract description 5
- 238000005452 bending Methods 0.000 abstract description 3
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 abstract 1
- -1 polyethylene Polymers 0.000 description 11
- 229920000139 polyethylene terephthalate Polymers 0.000 description 7
- 239000005020 polyethylene terephthalate Substances 0.000 description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000009998 heat setting Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000004408 titanium dioxide Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 239000004793 Polystyrene Substances 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
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- ACCCMOQWYVYDOT-UHFFFAOYSA-N hexane-1,1-diol Chemical compound CCCCCC(O)O ACCCMOQWYVYDOT-UHFFFAOYSA-N 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- BDJRBEYXGGNYIS-UHFFFAOYSA-N nonanedioic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-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
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 238000007666 vacuum forming Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 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
- NZZFYRREKKOMAT-UHFFFAOYSA-N diiodomethane Chemical compound ICI NZZFYRREKKOMAT-UHFFFAOYSA-N 0.000 description 1
- BTVWZWFKMIUSGS-UHFFFAOYSA-N dimethylethyleneglycol Natural products CC(C)(O)CO BTVWZWFKMIUSGS-UHFFFAOYSA-N 0.000 description 1
- 238000007688 edging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 229920001519 homopolymer Polymers 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
- 238000005192 partition Methods 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Polyesters Or Polycarbonates (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は成形加工用ポリエステルフィルムに関し、更に
詳しくは深絞り成形性、耐ピンホール性。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a polyester film for forming processing, and more specifically to deep drawing formability and pinhole resistance.
折曲げ性等に優れ、単独で、或は他の素材と貼合せた後
に、容器等に成形加工するのに特に有用な成形加工用ポ
リエステルフィルムに関する。The present invention relates to a polyester film for molding that has excellent bendability and is particularly useful for molding into containers and the like either alone or after being laminated with other materials.
〈従来技術とその問題点〉
プラスチックフィルムに真空成形、圧空成形等の深絞り
加工を施して容器等を製造することは従来より知られて
いる。そして、このフィルムとして通常ポリオレフィン
フィルム、ポリスチレンフィルム、ポリ塩化ビニルフィ
ルム、無延伸ポリエヂレンデレフタレートフイルム等が
用いられている。しかしながら、ポリオレフィン、ポリ
スチレン、ポリ塩化ビニルの最大の欠点は耐熱性が不足
することであり、多くは100℃以上では使用できない
。また無延伸ポリエチレンテレフタレートフィルムは1
00℃以上では結晶化現象が生じて透明性を失い、かつ
脆くなるという欠点がある。さらに、従来から使用され
てきたプラスチック素材の多(はガスバリヤ−性に量産
がある。<Prior art and its problems> It has been known for a long time to manufacture containers and the like by subjecting plastic films to deep drawing processing such as vacuum forming and pressure forming. As this film, polyolefin film, polystyrene film, polyvinyl chloride film, unstretched polyethylene derephthalate film, etc. are usually used. However, the biggest drawback of polyolefin, polystyrene, and polyvinyl chloride is that they lack heat resistance, and many cannot be used at temperatures above 100°C. In addition, unstretched polyethylene terephthalate film has 1
At temperatures above 00°C, crystallization occurs, resulting in loss of transparency and brittleness. Furthermore, many of the plastic materials that have been used in the past are being mass-produced due to their gas barrier properties.
〈問題を解決するための手段〉
木発明者は、かかる問題を解決すべく鋭意検討した結果
、本発明に到達した。<Means for Solving the Problem> As a result of intensive study to solve the problem, the inventor of the tree arrived at the present invention.
すなわち・、本発明は、平均粒径が2.5μm以下の滑
剤を含有し、融点が210〜245℃の共重合ポリエス
テルからなり、面配向係数が0.060〜0.110で
あることを特徴とする成形加工用ポリエステルフィルム
である。That is, the present invention is characterized in that it contains a lubricant with an average particle size of 2.5 μm or less, is made of a copolymerized polyester with a melting point of 210 to 245°C, and has a planar orientation coefficient of 0.060 to 0.110. This is a polyester film for molding.
本発明における共重合ポリニスデルとしては共重合ポリ
エ・チレンテレフタレートが代表例として挙げられる。A representative example of the copolymerized polynisdel in the present invention is copolymerized polyethylene terephthalate.
この共重合成分は酸成分でムアルコール成分でも良い。This copolymerization component may be an acid component or a mucoalcohol component.
該酸成分としてはイソフタル酸、フタル酸、ナフタレン
ジカルボン酸等の如き芳香族二塩基酸、アジピン酸、ア
ゼライン酸、セパチン酸、デカンジカルボン酸等の如き
脂肪族ジカルボン酸、シクロヘキサンジカルボン酸の如
き脂環族ジカルボン酸等が例示でき、またアルコール成
分としては、ブタンジオール、ヘキサンジオール、ネオ
ペンチルグリコール、ヘキサンジオール等の如き脂肪族
ジオール、シクロヘキサンジメタツールの如き脂環族ジ
オール等が例示できる。The acid component includes aromatic dibasic acids such as isophthalic acid, phthalic acid, and naphthalene dicarboxylic acid; aliphatic dicarboxylic acids such as adipic acid, azelaic acid, sepacic acid, and decane dicarboxylic acid; and alicyclic acids such as cyclohexane dicarboxylic acid. Examples of the alcohol component include aliphatic diols such as butanediol, hexanediol, neopentyl glycol, and hexanediol, and alicyclic diols such as cyclohexanedimetatool.
これらは単独または二種以上を使用することができる。These can be used alone or in combination of two or more.
共重合成分の割合は、その種類にもよるが結果としてポ
リマー融点が210〜245℃、好ましくは215〜2
40℃の範囲になる割合である。この融点が210℃未
満では成形加工時にクレージング(ひび割れ)が生じる
ので、好ましくない。また成形品に印刷を施すことが多
く、この印刷時の熱に耐えるためにも、210℃以上の
融点をもつことが必要ぐある。一方、融点が245℃を
超えると、例えば後述する面配向係数が所定の範囲内に
あっても、成形加工性が十分でなく、好ましくない。こ
こで、ポリエステルの融点測定は、セイコー電子(掬M
DSC−8SC/ 580を用い、昇温速度10℃/′
分で融解ピークを求める方法による。The proportion of copolymerized components depends on the type, but as a result, the polymer melting point is 210-245°C, preferably 215-245°C.
This is the ratio that results in a temperature range of 40°C. If the melting point is less than 210°C, crazing (cracking) will occur during molding, which is not preferable. Furthermore, since molded products are often printed, it is necessary to have a melting point of 210°C or higher in order to withstand the heat during printing. On the other hand, if the melting point exceeds 245° C., for example, even if the planar orientation coefficient described below is within a predetermined range, moldability will be insufficient, which is undesirable. Here, the melting point of polyester is measured using Seiko Electronics (Kiku M
Using DSC-8SC/580, heating rate 10℃/'
Depends on the method of determining the melting peak in minutes.
本発明における共重合ポリエステルは、平均粒径2.5
μm以下の滑剤を含有する。この滑剤は無機、有様系を
問わないが、無機系が好ましい、無機系滑剤としては、
シリカ、アルミナ、二酸化チタン、炭酸カルシウム、硫
酸バリウム等が例示でき、有機系滑剤としてはシリコー
ン粒子等が例示できる。いずれも平均粒径が2.5μm
以下であることを要する。滑剤の平均粒径が2.5μm
を越える場合には、真空成形等により深絞りされた部分
の、滑剤が起点となり、ピンホールを生じたり、場合に
よっては破断するので、好ましくない。The copolymerized polyester in the present invention has an average particle size of 2.5
Contains a lubricant of µm or less. This lubricant can be either inorganic or tangible, but inorganic lubricants are preferred.
Examples of such lubricants include silica, alumina, titanium dioxide, calcium carbonate, and barium sulfate, and examples of organic lubricants include silicone particles. Both have an average particle size of 2.5 μm.
The following must be true. Average particle size of lubricant is 2.5μm
If it exceeds this value, the lubricant in the deep-drawn part by vacuum forming etc. will become a starting point and cause pinholes or breakage in some cases, which is not preferable.
共重合ポリエステル中の滑剤の農は、フィルム製造工程
における巻取性によって決めるとよい。The quality of the lubricant in the copolyester may be determined by the winding properties in the film manufacturing process.
一般に粒径の大なるものは9吊、小なるものは多量添加
するのが好ましい。例えば、平均粒径2.3μmのシリ
カの場合は0.05重量%、平均粒径0.3μmの二酸
化チタンでは1重量%程度添加するのが好ましい。また
意図的に滑剤の含量を調整することにより、フィルムを
不透明化することもできる。例えば二酸化チタンを10
〜151m%添加することにより、白色のフィルムとす
ることができる。In general, it is preferable to add 9 particles if the particle size is large, and a large amount if the particle size is small. For example, in the case of silica with an average particle size of 2.3 μm, it is preferable to add 0.05% by weight, and in the case of titanium dioxide with an average particle size of 0.3 μm, it is preferable to add about 1% by weight. It is also possible to make the film opaque by intentionally adjusting the lubricant content. For example, titanium dioxide
By adding up to 151 m%, a white film can be obtained.
本発明における共重合ポリエステルは、その製法によっ
て限定されることはない。例えば、テレフタル酸、エチ
レングリコール及び共重合成分をエステル化反応させ、
次いで得られる反応生成物を重縮合反応させて共重合ポ
リニスデルとする方法、ジメチルテレフタレート、エチ
レングリコール及び共重合成分をエステル交換反応させ
、次いで得られる反応生成物を重縮合反応させて共重合
ポリエステルとする方法が好ましく用いられる。The copolymerized polyester in the present invention is not limited by its manufacturing method. For example, by esterifying terephthalic acid, ethylene glycol, and a copolymer component,
Next, the resulting reaction product is subjected to a polycondensation reaction to obtain a copolymerized polynisdel, and dimethyl terephthalate, ethylene glycol, and a copolymer component are transesterified, and the resulting reaction product is then subjected to a polycondensation reaction to form a copolymerized polyester. A method is preferably used.
また共重合成分から成るポリエステルをポリエチレンテ
レフタレートにブレンド後溶融し、分配反応により共重
合化する方法も採用し得る。共重合ポリエステルの製造
において必要に応じ、他の添加剤例えば酸化防止剤、熱
安定剤、紫外線吸収剤。Alternatively, a method may be adopted in which a polyester consisting of a copolymerized component is blended with polyethylene terephthalate, then melted, and copolymerized by a partition reaction. Other additives such as antioxidants, heat stabilizers, and ultraviolet absorbers may be added as necessary in the production of copolyester.
帯電防止剤等も添加することができる。Antistatic agents and the like can also be added.
本発明のポリエステルフィルムは、上記共重合ポリエス
テルを溶融し、ダイより吐出してフィルム状に成形し、
二輪延伸、熱固定したものであるが、該フィルムの面配
向係数はo、oeo以上0.110以下、好ましくは0
.070以上0.100以下であることを要する。面配
向係数が0.060未満では、折曲げに対し弱くなる、
例えば容器に成形後縁取りのため折曲げ加工(カーリン
グともいう)を行うと曲げられた部分が白化し、脆くな
るので、好ましくない。一方面配向係数が0.110を
超えた場合には、深絞りの成形が不十分となるので、好
ましくない。ここで、面配向係数とは、以下の式により
定義されるものである。The polyester film of the present invention is produced by melting the above-mentioned copolyester and extruding it from a die to form a film.
The film is two-wheel stretched and heat-set, and the plane orientation coefficient of the film is o, oeo or more and 0.110 or less, preferably 0.
.. It is required that the value is 070 or more and 0.100 or less. If the plane orientation coefficient is less than 0.060, it becomes weak against bending.
For example, if the container is bent (also called curling) for edging after being formed, the bent portion will turn white and become brittle, which is not preferable. If the one-plane orientation coefficient exceeds 0.110, deep drawing becomes insufficient, which is not preferable. Here, the planar orientation coefficient is defined by the following formula.
「−[(几x +nV )/2] −nl上記式におい
て、f :面配向係魯、nx 、 ny 。"-[(几x+nV)/2]-nl In the above formula, f: plane orientation ratio, nx, ny.
nl:それぞれ、フィルムの横、縦、厚さ方向の屈折率
である。なお、屈折率は以下のようにして測定する。nl: refractive index in the horizontal, vertical, and thickness directions of the film, respectively. Note that the refractive index is measured as follows.
アツベの屈折計の接眼側に偏光板アナライザーを取り付
け、単色光NaD線で、それぞれの屈折率を測定覆る。A polarizing plate analyzer is attached to the eyepiece side of Atsube's refractometer, and each refractive index is measured using a monochromatic NaD ray.
マウント液はヨウ化メチレンを用い、測定mt*は25
℃である。The mounting solution used was methylene iodide, and the measured mt* was 25
It is ℃.
上記面配向係数を得るには、逐次二次延伸において縦延
伸倍率を2.7〜3.5倍、横延伸倍率を3.0〜3.
6倍、熱固定温度を180〜220℃として延伸熱処理
するとよい。更に好ましく、かかる条件の中から面配向
係数が0.060以上0.110以下になる条件をみつ
けて、二輪延伸、熱固定処理を行うとよい。In order to obtain the above plane orientation coefficient, in the sequential secondary stretching, the longitudinal stretch ratio is 2.7 to 3.5 times, and the transverse stretch ratio is 3.0 to 3.
It is preferable to carry out stretching heat treatment at a heat setting temperature of 180 to 220°C. More preferably, the conditions under which the plane orientation coefficient is 0.060 or more and 0.110 or less are found, and the two-wheel stretching and heat setting treatments are performed.
本発明の目的は、上述した融点、滑剤、面配向係数の三
つの条件が全て満されて始めて達成されるものである。The object of the present invention is achieved only when all three conditions of the above-mentioned melting point, lubricant, and planar orientation coefficient are satisfied.
例えば、ポリエヂレンテレフタレートホモポリマーにて
滑剤条件2面配向係数条件が達成されても十分な深絞り
性は得られず、また滑剤の平均粒径が2.5μ風を越え
れば他の二つの条件が達成されてもピンホールを生じ、
トラブルの原因となってしまう。For example, even if the lubricant conditions and the dihedral orientation coefficient conditions are achieved with polyethylene terephthalate homopolymer, sufficient deep drawability cannot be obtained, and if the average particle size of the lubricant exceeds 2.5μ, the other two Even if the conditions are met, pinholes will occur,
It may cause trouble.
本発明のポリエステルフィルムは、厚みが6〜100μ
m1更には12〜38μmであることが好ましい。The polyester film of the present invention has a thickness of 6 to 100μ
It is more preferable that m1 is 12 to 38 μm.
〈実施例〉 以下、実施例を掲げて本発明を更に説明する。<Example> The present invention will be further explained below with reference to Examples.
実施例1及び比較例1,2
平均粒径2.0μmのシリカ0.07重8%を添加含有
する、イソフタル912モル%共重合ポリエチレンテレ
フタレート(融点229℃、固有粘度0.60 )を2
10℃で溶融押出し、急冷固化して厚さ700μmの未
延伸フィルムを得た。次いで、この未延伸フィルムを、
第1表に示す条件で、縦延伸し、横延伸し、続いて熱固
定処理して二軸配向フィルムを得た。Example 1 and Comparative Examples 1 and 2 912 mol% isophthalic copolymerized polyethylene terephthalate (melting point 229°C, intrinsic viscosity 0.60) containing 0.07 wt 8% silica with an average particle size of 2.0 μm (melting point 229°C, intrinsic viscosity 0.60)
It was melt-extruded at 10° C. and rapidly solidified to obtain an unstretched film with a thickness of 700 μm. Next, this unstretched film is
Under the conditions shown in Table 1, the film was longitudinally stretched, transversely stretched, and then heat-set to obtain a biaxially oriented film.
このフィルムの特性を第4表に示す。The properties of this film are shown in Table 4.
第1表
実施例2及び比較例3〜6
平均粒径2.3μmのシリカ0.05重間%を添加含有
し、第2表に示す成分を共重合した共重合ポリエチレン
テレフタレート(固有粘度0.60 )を第2表に示す
温度で溶融押出し、急冷固化して未延伸フィルム(厚さ
二800μm)を得た。次いで、この未延伸フィルムを
、第2表に示す条件で、縦延伸し、横延伸し、続いて熱
固定処理して二軸配向フィルムを得た。Table 1 Example 2 and Comparative Examples 3 to 6 Copolymerized polyethylene terephthalate containing 0.05% by weight of silica with an average particle size of 2.3 μm and copolymerized with the components shown in Table 2 (intrinsic viscosity 0. 60) was melt-extruded at the temperature shown in Table 2 and rapidly solidified to obtain an unstretched film (thickness: 2,800 μm). Next, this unstretched film was longitudinally stretched and transversely stretched under the conditions shown in Table 2, followed by heat setting treatment to obtain a biaxially oriented film.
このフィルムの特性を第4表に示す。The properties of this film are shown in Table 4.
第2表
実施例3.4及び比較例7
第3表に示す滑剤を添加含有する、イソフタル酸12モ
ル%共重合ポリエチレンテレフタレート(固有粘度0.
60 )を270℃で溶融押出し、急冷固化して未延伸
フィルムとし、次いで該未延伸フィルムを縦延伸温度8
0℃、ii延伸倍率3.3倍、横延伸温度110℃、横
延伸倍率3.5倍で逐次二輪延卸し、次いで210℃で
熱固定した。Table 2 Example 3.4 and Comparative Example 7 Polyethylene terephthalate copolymerized with 12 mol % of isophthalic acid (intrinsic viscosity: 0.5%) containing the lubricant shown in Table 3.
60) was melt-extruded at 270°C, rapidly cooled and solidified to form an unstretched film, and then the unstretched film was longitudinally stretched at a temperature of 8.
Two-wheel stretching was carried out successively at 0° C., ii. draw ratio: 3.3 times, transverse drawing temperature: 110° C., and transverse drawing ratio: 3.5 times, followed by heat setting at 210° C.
1qられた二軸配向フィルム(厚み=50μm )の特
性を第4表に示す。Table 4 shows the properties of the biaxially oriented film (thickness = 50 μm).
第3表
ト記実施例1〜4.比較例1〜7で得られた計11種の
フィルムくいずれも中600#1llI>を夫々IRヒ
ーターで10秒間加熱し、フィルムの温度を130℃に
した後ロ径10履、底径55. 、深さ80繻の金属金
型上に置き、圧力5 K9 / cdで圧空成形を行な
った。次いで、カップ状物の縁を切り離し、縁部のカー
リング加工を行なってカップを成形した。Table 3 Examples 1 to 4. A total of 11 types of films obtained in Comparative Examples 1 to 7 were heated with an IR heater for 10 seconds to bring the temperature of the film to 130°C. It was placed on a metal mold with a depth of 80 mm, and air pressure molded at a pressure of 5 K9/cd. Next, the edges of the cup-shaped article were cut off, and the edges were curled to form a cup.
この成形に於て、圧空成形時に
○:フイルムにクラックを生じなかった×:フィルムに
クラックを生じた
また、カーリング加工に於て
O:縁部にひび割れを生じなかった
×:縁部にひび割れを生じた
の2点を評価した結果を第4表に示す。In this molding, ○: no cracks were formed in the film during pressure forming; ×: cracks were formed in the film; and during curling processing, O: no cracks were formed at the edges; Table 4 shows the results of evaluating the two points that occurred.
第4表
第4表の結果から、実施例のフィルムが深絞り性、縁取
りカーリング性等にすぐれていることがわかる。From the results shown in Table 4, it can be seen that the films of Examples are excellent in deep drawing properties, edge curling properties, etc.
〈発明の効果〉
本発明のポリエステルフィルムは耐ピンホール性、深絞
り成形性、折曲げ加工性等に優れ、成形加工用特に単独
、或は他の素材例えばプラスチック、金属板等と貼合せ
た後の容器等の深絞り成形用として優れたものである。<Effects of the Invention> The polyester film of the present invention has excellent pinhole resistance, deep drawing formability, bending workability, etc., and is suitable for molding, especially alone or laminated with other materials such as plastics, metal plates, etc. It is excellent for later deep drawing of containers, etc.
Claims (1)
〜245℃の共重合ポリエステルからなり、面配向係数
が0.060〜0.110であることを特徴とする成形
加工用ポリエステルフィルム。Contains a lubricant with an average particle size of 2.5 μm or less and has a melting point of 210
A polyester film for molding, which is made of a copolymerized polyester at a temperature of ~245°C and has a planar orientation coefficient of 0.060 to 0.110.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1126730A JPH0819245B2 (en) | 1989-05-22 | 1989-05-22 | Polyester film for container molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1126730A JPH0819245B2 (en) | 1989-05-22 | 1989-05-22 | Polyester film for container molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02305827A true JPH02305827A (en) | 1990-12-19 |
JPH0819245B2 JPH0819245B2 (en) | 1996-02-28 |
Family
ID=14942459
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1126730A Expired - Fee Related JPH0819245B2 (en) | 1989-05-22 | 1989-05-22 | Polyester film for container molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0819245B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0393525A (en) * | 1989-09-06 | 1991-04-18 | Toyobo Co Ltd | Polyester film for lamination of metal |
JPH0671747A (en) * | 1992-08-31 | 1994-03-15 | Teijin Ltd | Polyester film for laminating metallic sheet |
US5882784A (en) * | 1994-12-16 | 1999-03-16 | Toray Industries, Inc. | Metal-film laminate |
EP1002827A1 (en) * | 1998-11-20 | 2000-05-24 | Toray Industries, Inc. | Formable biaxially-oriented polyester film |
JP2001121615A (en) * | 2000-09-25 | 2001-05-08 | Toyo Kohan Co Ltd | Method for manufacturing resin-coated metallic plate |
JP2004362953A (en) * | 2003-06-05 | 2004-12-24 | Toray Ind Inc | Polyester film for lithium battery packing |
WO2005023910A1 (en) * | 2003-09-02 | 2005-03-17 | Toyo Boseki Kabushiki Kaisha | Polyester film for forming |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5935344A (en) * | 1982-08-21 | 1984-02-27 | ダニ−ル・ジヨセフ・ブラツドリ− | Electro-optical image tube and method of operating same |
JPS6221428A (en) * | 1985-07-19 | 1987-01-29 | Toyo Seikan Kaisha Ltd | Manufacture of deep draw forming container |
JPS6261427A (en) * | 1985-09-12 | 1987-03-18 | Canon Inc | Coding system |
JPS6440400A (en) * | 1987-08-06 | 1989-02-10 | Diafoil Co Ltd | Polyester film for transfer film |
JPH02204020A (en) * | 1989-02-01 | 1990-08-14 | Diafoil Co Ltd | Biaxially stretched polyester film for forming, formed-transferring film and formed container |
-
1989
- 1989-05-22 JP JP1126730A patent/JPH0819245B2/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5935344A (en) * | 1982-08-21 | 1984-02-27 | ダニ−ル・ジヨセフ・ブラツドリ− | Electro-optical image tube and method of operating same |
JPS6221428A (en) * | 1985-07-19 | 1987-01-29 | Toyo Seikan Kaisha Ltd | Manufacture of deep draw forming container |
JPS6261427A (en) * | 1985-09-12 | 1987-03-18 | Canon Inc | Coding system |
JPS6440400A (en) * | 1987-08-06 | 1989-02-10 | Diafoil Co Ltd | Polyester film for transfer film |
JPH02204020A (en) * | 1989-02-01 | 1990-08-14 | Diafoil Co Ltd | Biaxially stretched polyester film for forming, formed-transferring film and formed container |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0393525A (en) * | 1989-09-06 | 1991-04-18 | Toyobo Co Ltd | Polyester film for lamination of metal |
JPH0671747A (en) * | 1992-08-31 | 1994-03-15 | Teijin Ltd | Polyester film for laminating metallic sheet |
US5882784A (en) * | 1994-12-16 | 1999-03-16 | Toray Industries, Inc. | Metal-film laminate |
EP1002827A1 (en) * | 1998-11-20 | 2000-05-24 | Toray Industries, Inc. | Formable biaxially-oriented polyester film |
JP2001121615A (en) * | 2000-09-25 | 2001-05-08 | Toyo Kohan Co Ltd | Method for manufacturing resin-coated metallic plate |
JP2004362953A (en) * | 2003-06-05 | 2004-12-24 | Toray Ind Inc | Polyester film for lithium battery packing |
JP4543626B2 (en) * | 2003-06-05 | 2010-09-15 | 東レ株式会社 | Polyester film for lithium battery packaging |
WO2005023910A1 (en) * | 2003-09-02 | 2005-03-17 | Toyo Boseki Kabushiki Kaisha | Polyester film for forming |
US7198857B2 (en) | 2003-09-02 | 2007-04-03 | Toyo Boseki Kabushiki Kaisha | Polyester film for forming |
Also Published As
Publication number | Publication date |
---|---|
JPH0819245B2 (en) | 1996-02-28 |
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