JPH11138629A - Co-biaxially stretched polyester film and manufacturing thereof - Google Patents
Co-biaxially stretched polyester film and manufacturing thereofInfo
- Publication number
- JPH11138629A JPH11138629A JP9318989A JP31898997A JPH11138629A JP H11138629 A JPH11138629 A JP H11138629A JP 9318989 A JP9318989 A JP 9318989A JP 31898997 A JP31898997 A JP 31898997A JP H11138629 A JPH11138629 A JP H11138629A
- Authority
- JP
- Japan
- Prior art keywords
- stretching
- film
- polyester film
- temperature
- ratio
- 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 abstract description 35
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- 238000001069 Raman spectroscopy Methods 0.000 claims abstract description 20
- 230000009477 glass transition Effects 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 17
- 238000000790 scattering method Methods 0.000 claims abstract description 16
- -1 polyethylene terephthalate Polymers 0.000 claims description 27
- 229920000728 polyester Polymers 0.000 claims description 19
- 238000002844 melting Methods 0.000 claims description 18
- 230000008018 melting Effects 0.000 claims description 18
- 230000005291 magnetic effect Effects 0.000 claims description 15
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 14
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 14
- 239000003990 capacitor Substances 0.000 claims description 9
- 238000012546 transfer Methods 0.000 claims description 7
- 229920001577 copolymer Polymers 0.000 claims description 6
- 239000013078 crystal Substances 0.000 claims description 5
- 230000004927 fusion Effects 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 2
- 229920003207 poly(ethylene-2,6-naphthalate) Polymers 0.000 claims description 2
- 239000011112 polyethylene naphthalate Substances 0.000 claims description 2
- 239000002245 particle Substances 0.000 description 21
- 239000008188 pellet Substances 0.000 description 16
- 238000001816 cooling Methods 0.000 description 15
- 238000005259 measurement Methods 0.000 description 12
- 238000012360 testing method Methods 0.000 description 10
- 239000010410 layer Substances 0.000 description 9
- 239000004793 Polystyrene Substances 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 229920002223 polystyrene Polymers 0.000 description 8
- 238000001291 vacuum drying Methods 0.000 description 8
- 238000009998 heat setting Methods 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 5
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N methyl ethyl ketone Substances CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 5
- YXFVVABEGXRONW-UHFFFAOYSA-N toluene Substances CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 4
- 239000006229 carbon black Substances 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000003973 paint Substances 0.000 description 4
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 4
- 230000010287 polarization Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 4
- 230000003746 surface roughness Effects 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 150000002009 diols Chemical class 0.000 description 3
- 229920001971 elastomer Polymers 0.000 description 3
- 239000000696 magnetic material Substances 0.000 description 3
- 239000011146 organic particle Substances 0.000 description 3
- 229920002635 polyurethane Polymers 0.000 description 3
- 239000004814 polyurethane 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
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 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
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 239000001361 adipic acid Substances 0.000 description 2
- 235000011037 adipic acid Nutrition 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- AYJRCSIUFZENHW-UHFFFAOYSA-L barium carbonate Chemical compound [Ba+2].[O-]C([O-])=O AYJRCSIUFZENHW-UHFFFAOYSA-L 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
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 239000001506 calcium phosphate Substances 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 239000012770 industrial material Substances 0.000 description 2
- 239000010954 inorganic particle Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 125000005395 methacrylic acid group Chemical group 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- 235000012771 pancakes Nutrition 0.000 description 2
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- GZVHEAJQGPRDLQ-UHFFFAOYSA-N 6-phenyl-1,3,5-triazine-2,4-diamine Chemical compound NC1=NC(N)=NC(C=2C=CC=CC=2)=N1 GZVHEAJQGPRDLQ-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 1
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- ORLQHILJRHBSAY-UHFFFAOYSA-N [1-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1(CO)CCCCC1 ORLQHILJRHBSAY-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 229910002113 barium titanate Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- YYRMJZQKEFZXMX-UHFFFAOYSA-L calcium bis(dihydrogenphosphate) Chemical compound [Ca+2].OP(O)([O-])=O.OP(O)([O-])=O YYRMJZQKEFZXMX-UHFFFAOYSA-L 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- FUFJGUQYACFECW-UHFFFAOYSA-L calcium hydrogenphosphate Chemical compound [Ca+2].OP([O-])([O-])=O FUFJGUQYACFECW-UHFFFAOYSA-L 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 238000003490 calendering Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 239000003484 crystal nucleating agent Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 235000019700 dicalcium phosphate Nutrition 0.000 description 1
- 229940095079 dicalcium phosphate anhydrous Drugs 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000005294 ferromagnetic effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical group FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 238000001459 lithography Methods 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000005058 metal casting Methods 0.000 description 1
- 238000001465 metallisation Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 235000019691 monocalcium phosphate Nutrition 0.000 description 1
- 229910000150 monocalcium phosphate Inorganic materials 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 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
- RXOHFPCZGPKIRD-UHFFFAOYSA-N naphthalene-2,6-dicarboxylic acid Chemical compound C1=C(C(O)=O)C=CC2=CC(C(=O)O)=CC=C21 RXOHFPCZGPKIRD-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920000874 polytetramethylene terephthalate Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000003578 releasing effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Landscapes
- Printing Plates And Materials Therefor (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Thermal Transfer Or Thermal Recording In General (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、同時二軸延伸ポリ
エステルフィルムおよびその製造方法に関し、特に縦横
方向に高強度化され、各種工業材料フィルムに適した同
時二軸延伸ポリエステルフィルムおよびその製造方法に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a simultaneous biaxially stretched polyester film and a method for producing the same, and more particularly to a simultaneous biaxially stretched polyester film which has high strength in the longitudinal and transverse directions and is suitable for various industrial material films. .
【0002】[0002]
【従来の技術】プラスチックフィルムは、他の素材から
は得られないような大面積のフィルムの連続生産が可能
であり、その強度、耐久性、透明性、柔軟性、表面特性
の付与などの特徴を活かして、農業用、包装用、建材用
などの大量に需要のある分野で用いられている。中で
も、二軸延伸ポリエステルフィルムは、その優れた機械
的特性、熱的特性、電気的特性、耐薬品性のために、さ
まざまな分野で利用されており、特に磁気テープ用ベー
スフィルムとしての有用性は、他のフィルムの追随を許
さない。近年は機材の軽量化、小型化と長時間記録化の
ためにベースフィルムの一層の薄膜化が要求され、従っ
てますますの高強度化が望まれている。2. Description of the Related Art Plastic films enable continuous production of large-area films that cannot be obtained from other materials, and are characterized by their strength, durability, transparency, flexibility, and imparting surface characteristics. Utilizing it, it is used in fields that are in large demand, such as for agriculture, packaging, and building materials. Among them, biaxially stretched polyester films are used in various fields because of their excellent mechanical properties, thermal properties, electrical properties, and chemical resistance, and are particularly useful as base films for magnetic tape. Is unrivaled by other films. In recent years, the base film has been required to be thinner in order to reduce the weight and size of the equipment and to record for a long period of time, and accordingly, higher strength is desired.
【0003】また、熱転写リボン用、コンデンサ用、感
熱孔版印刷原紙用においても薄膜化の傾向が近年非常に
強く、同様にますますの高強度化が望まれている。In recent years, the tendency of thinning has been very strong in thermal transfer ribbons, capacitors, and heat-sensitive stencil printing papers in recent years, and similarly, higher strength is desired.
【0004】二軸延伸ポリエステルフィルムの高強度化
の手法としては、縦・横二方向に延伸したフィルムを再
度縦方向に延伸し、縦方向に高強度化するいわゆる再縦
延伸法が一般的である(例えば、特公昭42−9270
号公報、特公昭43−3040号公報、特開昭46−1
119号公報、特開昭46−1120号公報)。また、
さらに横方向にも強度を付与したい場合には、再縦延伸
を行なった後、再度横方向に延伸する再縦再横延伸法が
提案されている(例えば、特開昭50−133276号
公報、特開昭55−22915号公報)。As a technique for increasing the strength of a biaxially stretched polyester film, a so-called re-longitudinal stretching method in which a film stretched in two longitudinal and transverse directions is stretched again in the longitudinal direction to increase the strength in the longitudinal direction is generally used. (For example, Japanese Patent Publication No. 42-9270)
JP, JP-B-43-3040, JP-A-46-1
119, JP-A-46-1120). Also,
In order to further impart strength in the horizontal direction, a re-longitudinal re-horizontal stretching method has been proposed in which the film is stretched again in the transverse direction and then stretched in the transverse direction again (for example, JP-A-50-133276, JP-A-55-22915).
【0005】[0005]
【発明が解決しようとする課題】縦横方向に高強度され
た二軸延伸ポリエステルフィルムを得るための手法とし
ては、上記のような従来の再縦再横延伸法などがある
が、再縦延伸して縦方向に高強度化した後、再横延伸し
て横方向を高強度化すると、縦方向の配向が低下する欠
点があり、縦横方向を同時に高強度化するのが難かし
く、延伸時のフィルム破れ頻度が高くなる。As a technique for obtaining a biaxially stretched polyester film having a high strength in the machine and transverse directions, there is the above-mentioned conventional re-mechanical re-horizontal stretching method. After increasing the strength in the vertical direction, and then re-horizontal stretching to increase the strength in the horizontal direction, there is a disadvantage that the orientation in the vertical direction decreases, and it is difficult to increase the strength in the vertical and horizontal directions at the same time. The frequency of film tearing increases.
【0006】本発明の課題は、縦横方向の配向が大き
く、高強度化された同時二軸延伸ポリエステルフィルム
およびその製造方法を提供することにある。An object of the present invention is to provide a simultaneously biaxially stretched polyester film having a large orientation in the vertical and horizontal directions and a high strength, and a method for producing the same.
【0007】[0007]
【課題を解決するための手段】上記課題を解決するため
に、本発明の同時二軸延伸ポリエステルフィルムの製造
方法は、未延伸キャストフィルムを、(ポリエステルの
ガラス転移温度Tg+25)℃〜(Tg+45)℃の温
度範囲で面積延伸倍率2〜7倍で縦および横方向に同時
二軸延伸する第1段目の延伸工程と、引続き(Tg−1
5)℃〜(Tg+10)℃の温度範囲で面積延伸倍率4
〜20倍で縦および横方向に同時二軸延伸する第2段目
の延伸工程を有することを特徴とする方法からなる。In order to solve the above-mentioned problems, a method for producing a simultaneously biaxially stretched polyester film of the present invention comprises the steps of: forming an unstretched cast film from (glass transition temperature of polyester Tg + 25) ° C. to (Tg + 45) A first stretching step of simultaneous biaxial stretching in the longitudinal and transverse directions at an area stretching magnification of 2 to 7 times in a temperature range of ° C, and subsequently (Tg-1
5) Area stretching ratio of 4 in the temperature range of ° C to (Tg + 10) ° C.
The method is characterized in that it has a second stretching step of simultaneously biaxially stretching in the vertical and horizontal directions at up to 20 times.
【0008】また、本発明に係る同時二軸延伸ポリエス
テルフィルムの製造方法は、未延伸キャストフィルム
を、(ポリエステルのガラス転移温度Tg+25)℃〜
(Tg+45)℃の温度範囲で面積延伸倍率2〜7倍で
縦および横方向に同時二軸延伸する第1段目の延伸工程
と、引続き(Tg−15)℃〜(Tg+10)℃の温度
範囲で面積延伸倍率4〜16倍で縦および横方向に同時
二軸延伸する第2段目の延伸工程と、さらに(ポリエス
テルの融解温度Tm−130)℃〜(Tm−10)℃の
温度範囲で面積延伸倍率1.5〜5倍で縦および横方向
に同時二軸延伸する第3段目の延伸工程を有することを
特徴とする方法からなる。Further, the method for producing a simultaneously biaxially stretched polyester film according to the present invention is characterized in that the unstretched cast film is formed by (polyester glass transition temperature Tg + 25) ° C.
The first-stage stretching step of simultaneous biaxial stretching in the longitudinal and transverse directions at an area stretching ratio of 2 to 7 in the temperature range of (Tg + 45) ° C., and subsequently in the temperature range of (Tg−15) ° C. to (Tg + 10) ° C. And a second stretching step of simultaneously biaxially stretching in the longitudinal and transverse directions at an area stretching ratio of 4 to 16 times, and further in a temperature range of (melting temperature of polyester Tm-130) ° C to (Tm-10) ° C. The method comprises a third-stage stretching step of simultaneous biaxial stretching in the longitudinal and transverse directions at an area stretching ratio of 1.5 to 5 times.
【0009】また、本発明に係る同時二軸延伸ポリエス
テルフィルムは、同時二軸延伸後の、レーザーラマン散
乱法で測定した1615cm-1における縦方向のピーク
強度(IMD)と厚み方向のピーク強度(IND)との比R
1 (=IMD/IND)と横方向のピーク強度(ITD)と厚
み方向のピーク強度(IND)との比R2 (=ITD/
IND)の少なくともいずれか一方が6以上であることを
特徴とするものからなる。Further, simultaneous biaxial oriented polyester film according to the present invention, after the simultaneous biaxial stretching, the peak intensity in the longitudinal direction of the peak intensity (I MD) and thickness direction at 1615 cm -1 measured by laser Raman scattering method Ratio R to (I ND )
The ratio R 2 (= I TD / 1 ) between 1 (= I MD / I ND ), the peak intensity in the lateral direction (I TD ), and the peak intensity in the thickness direction (I ND )
I ND ) is at least one of 6 or more.
【0010】[0010]
【発明の実施の形態】以下、本発明について、望ましい
実施の形態とともに詳細に説明する。本発明におけるレ
ーザーラマン散乱法で測定した1615cm-1における
縦方向のピーク強度(IMD)と厚み方向のピーク強度
(IND)との比R1 (=IMD/IND)と横方向のピーク
強度(ITD)と厚み方向のピーク強度(IND)との比R
2 (=ITD/IND)は、縦あるいは横方向の配向の強さ
を示す指標であるが、本発明で使用する1615cm-1
のラマンバンドはベンゼン環のC=C伸縮振動(νC=
C)に帰属されるバンドで、このバンドの強度は、ベン
ゼン環のパッキング状態によっても変化し、特に二軸延
伸フィルムの場合、配向のみでは決らないものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail together with preferred embodiments. The ratio R 1 (= I MD / I ND ) between the peak intensity (I MD ) in the longitudinal direction and the peak intensity (I ND ) in the thickness direction at 1615 cm −1 measured by the laser Raman scattering method in the present invention, and the ratio in the horizontal direction. the ratio R of the peak intensity between (I TD) and thickness direction of the peak intensity (I ND)
2 (= I TD / I ND ) is an index indicating the strength of vertical or horizontal orientation, and is 1615 cm −1 used in the present invention.
Raman band of C = C stretching vibration of benzene ring (νC =
In the band belonging to C), the intensity of this band varies depending on the packing state of the benzene ring, and particularly in the case of a biaxially stretched film, it cannot be determined only by the orientation.
【0011】本発明においては、高配向で高強度化され
たフィルムを得るために、この縦と横の強度比R1 、R
2 の少なくともいずれか一方が6以上であることが必要
である。好ましくは7以上である。特に、磁気材料用と
しては横方向の強度比R2 が6以上であることがさらに
好ましい。In the present invention, in order to obtain a film having a high orientation and a high strength, the strength ratios R 1 , R
It is necessary that at least one of 2 is 6 or more. Preferably it is 7 or more. In particular, for magnetic materials, it is more preferable that the lateral strength ratio R 2 is 6 or more.
【0012】また、通常の市販されている二軸延伸ポリ
エステルフィルムの縦方向のヤング率(EMD)、横方向
のヤング率(ETD)は4〜4.5GPaが普通である
が、磁気テープ用ベースフィルムでは、特に高出力化、
リボン用、感熱孔版印刷原紙用では高精細化、コンデン
サー用では、絶縁特性の向上、という目的を顕著に達成
するために、縦方向のヤング率(EMD)と横方向のヤン
グ率(ETD)の少なくともいずれか一方を6GPa以上
とすることが好ましい。さらに好ましくは7GPa以上
がより望ましい。この場合、ヤング率が6GPa未満と
なる方向のヤング率は5GPa以上とするのが好まし
い。A commercially available biaxially stretched polyester film usually has a Young's modulus (E MD ) in the machine direction and a Young's modulus (E TD ) in the transverse direction of 4 to 4.5 GPa. For base films for
In order to achieve the objectives of high definition for ribbons and heat-sensitive stencil printing paper, and to improve insulation properties for capacitors, the Young's modulus in the vertical direction (E MD ) and the Young's modulus in the horizontal direction (E TD ) have been achieved. ) Is preferably at least 6 GPa. More preferably, it is more preferably 7 GPa or more. In this case, the Young's modulus in the direction in which the Young's modulus is less than 6 GPa is preferably 5 GPa or more.
【0013】また、本発明で言うポリエステルとは、ジ
オールとジカルボン酸とからの縮重合により得られるポ
リマーである。ジカルボン酸とは、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、アジピ
ン酸、セバチン酸などで代表されるものであり、また、
ジオールとは、エチレングリコール、トリメチレングリ
コール、テトラメチレングリコール、シクロヘキサンジ
メタノールなどで代表されるものである。具体的には、
例えば、ポリメチレンテレフタレート、ポリエチレンテ
レフタレート、ポリプロピレンテレフタレート、ポリエ
チレンイソフタレート、ポリテトラメチレンテレフタレ
ート、ポリエチレン−p−オキシベンゾエート、ポリ−
1,4−シクロヘキシレンジメチレンテレフタレート、
ポリエチレン−2,6−ナフタレートなどを用いること
ができる。もちろん、これらのポリエステルは、ホモポ
リマーであってもコポリマーであってもよく、共重合成
分としては、例えば、ジエチレングリコール、ネオペン
チルグリコール、ポリアルキレングリコールなどのジオ
ール成分、アジピン酸、セバチン酸、フタル酸、イソフ
タル酸、2,6−ナフタレンジカルボン酸などのジカル
ボン酸成分を用いることができる。本発明の場合、特
に、ポリエチレンテレフタレート、ポリプロピレンテレ
フタレート、ポリエチレンイソフタレート、ポリエチレ
ンナフタレート(ポリエチレン−2,6−ナフタレー
ト)およびこれらの共重合体より選ばれた少なくとも一
種であることが機械的強度、耐熱性、耐薬品性、耐久性
などの観点から好ましい。The polyester in the present invention is a polymer obtained by condensation polymerization of a diol and a dicarboxylic acid. Dicarboxylic acids are represented by terephthalic acid, isophthalic acid, phthalic acid, naphthalenedicarboxylic acid, adipic acid, sebacic acid, etc.,
The diol is represented by ethylene glycol, trimethylene glycol, tetramethylene glycol, cyclohexanedimethanol and the like. In particular,
For example, polymethylene terephthalate, polyethylene terephthalate, polypropylene terephthalate, polyethylene isophthalate, polytetramethylene terephthalate, polyethylene-p-oxybenzoate, poly-
1,4-cyclohexylene dimethylene terephthalate,
Polyethylene-2,6-naphthalate or the like can be used. Of course, these polyesters may be homopolymers or copolymers. Examples of copolymerization components include diol components such as diethylene glycol, neopentyl glycol, and polyalkylene glycol, adipic acid, sebacic acid, and phthalic acid. And dicarboxylic acid components such as isophthalic acid and 2,6-naphthalenedicarboxylic acid. In the case of the present invention, at least one selected from polyethylene terephthalate, polypropylene terephthalate, polyethylene isophthalate, polyethylene naphthalate (polyethylene-2,6-naphthalate) and a copolymer thereof has mechanical strength and heat resistance. It is preferable from the viewpoints of properties, chemical resistance, durability and the like.
【0014】また、このポリエステルの中には、無機粒
子や有機粒子、その他の各種添加剤、例えば酸化防止
剤、帯電防止剤、結晶核剤などを添加してもかまわな
い。The polyester may contain inorganic particles, organic particles, and other various additives such as an antioxidant, an antistatic agent, and a crystal nucleating agent.
【0015】無機粒子の具体例としては、酸化ケイ素、
酸化アルミニウム、酸化マグネシウム、酸化チタンなど
の酸化物、カオリン、タルク、モンモリロナイトなどの
複合酸化物、炭酸カルシウム、炭酸バリウムなどの炭酸
塩、硫酸カルシウム、硫酸バリウムなどの硫酸塩、チタ
ン酸バリウム、チタン酸カリウムなどのチタン酸塩、リ
ン酸第3カルシウム、リン酸第2カルシウム、リン酸第
1カルシウムなどのリン酸塩などを用いることができる
が、これらに限定されるわけではない。また、これらは
目的に応じて2種以上用いてもかまわない。Specific examples of the inorganic particles include silicon oxide,
Oxides such as aluminum oxide, magnesium oxide, and titanium oxide; complex oxides such as kaolin, talc, and montmorillonite; carbonates such as calcium carbonate and barium carbonate; sulfates such as calcium sulfate and barium sulfate; barium titanate; Titanate such as potassium, phosphate such as tertiary calcium phosphate, dibasic calcium phosphate, and monocalcium phosphate can be used, but not limited thereto. These may be used in combination of two or more depending on the purpose.
【0016】有機粒子の具体例としては、ポリスチレン
もしくは架橋ポリスチレン粒子、スチレン・アクリル系
及びアクリル系架橋粒子、スチレン・メタクリル系及び
メタクリル系架橋粒子などのビニル系粒子、ベンゾグア
ナミン・ホルムアルデヒド、シリコーン、ポリテトラフ
ルオロエチレンなどの粒子を用いることができるが、こ
れらに限定されるものではなく、粒子を構成する部分の
うち少なくとも一部がポリエステルに対し不溶の有機高
分子微粒子であれば如何なる粒子でも良い。また有機粒
子は、易滑性、フィルム表面の突起形成の均一性から粒
子形状が球形状で均一な粒度分布のものが好ましい。Specific examples of the organic particles include polystyrene or crosslinked polystyrene particles, vinyl particles such as styrene / acrylic / acrylic crosslinked particles, styrene / methacrylic / methacrylic crosslinked particles, benzoguanamine / formaldehyde, silicone, and polytetrafluoroethylene. Although particles such as fluoroethylene can be used, the particles are not limited thereto, and any particles may be used as long as at least a part of the particles constituting the particles is organic polymer fine particles insoluble in polyester. The organic particles preferably have a spherical particle shape and a uniform particle size distribution from the viewpoint of smoothness and uniformity of formation of projections on the film surface.
【0017】これらの粒子の粒径、配合量、形状などは
用途、目的に応じて選ぶことが可能であるが、通常は、
平均粒子径としては0.05μm以上3μm以下、配合
量としては、0.01重量%以上10重量%以下が好ま
しい。The particle size, blending amount, shape and the like of these particles can be selected according to the application and purpose.
The average particle diameter is preferably 0.05 μm or more and 3 μm or less, and the blending amount is preferably 0.01% by weight or more and 10% by weight or less.
【0018】また、本発明のフィルムは2層以上の積層
フィルムであっても構わない。2層以上積層された積層
フィルムとするのは、特に磁気記録媒体のベースフィル
ムにおいて、用途に応じて、磁気記録面となるフィルム
面とその反対面の表面粗さを異なる設計にする方法とし
て最適である。The film of the present invention may be a laminated film having two or more layers. The use of a laminated film having two or more layers is particularly suitable for a base film of a magnetic recording medium, as a method of designing the surface roughness of a film surface to be a magnetic recording surface and a surface roughness different from each other depending on the application. It is.
【0019】本発明のフィルムは同時二軸延伸ポリエス
テルフィルムであり、所望のフィルムの配向の付与が本
発明の同時二軸延伸の製造方法によって達成されるもの
である。The film of the present invention is a simultaneously biaxially stretched polyester film, and the desired orientation of the film is imparted by the method of the present invention for simultaneous biaxially stretching.
【0020】本発明におけるフィルムの全体厚みは用
途、目的に応じて適宜決定することができる。通常磁気
材料用途では1μm以上20μm以下が好ましく、中で
もディジタルビデオ用塗布型磁気記録媒体用途では2μ
m以上8μm以下、ディジタルビデオ用蒸着型磁気記録
媒体用途では3μm以上9μm以下が好ましい。The total thickness of the film in the present invention can be appropriately determined according to the application and purpose. Normally, the thickness is preferably 1 μm or more and 20 μm or less for magnetic materials, and especially 2 μm for coating magnetic recording media for digital video.
m or more and 8 μm or less, and 3 μm or more and 9 μm or less for vapor deposition type magnetic recording media for digital video.
【0021】また、工業材料用途の中では、熱転写リボ
ン用途では1μm以上6μm以下、コンデンサ用途では
0.5μm以上15μm以下、感熱孔版原紙用途では
0.5μm以上5μm以下であることが好ましい。Further, among industrial materials, the thickness is preferably 1 μm to 6 μm for thermal transfer ribbons, 0.5 μm to 15 μm for capacitors, and 0.5 μm to 5 μm for heat-sensitive stencil paper.
【0022】本発明のレーザーラマン散乱法による強度
比Rが縦方向と横方向の少なくともいずれか一方が6以
上であるフィルムは、磁気媒体用途、熱転写リボン用
途、コンデンサ用途、感熱孔版印刷原紙用途などに好ま
しく用いることができる。The film having an intensity ratio R by the laser Raman scattering method of the present invention of at least one of the longitudinal direction and the transverse direction of 6 or more is used for magnetic media, heat transfer ribbon, capacitor, heat-sensitive stencil printing paper, etc. Can be preferably used.
【0023】磁気媒体用途の場合は、レーザーラマン散
乱法による強度比Rが縦方向と横方向の少なくともいず
れか一方が6以上であり、特に横方向の強度比R2 が6
以上、より好ましくは7以上とするのがより好ましい。
また、好ましくはフィルムの横方向のヤング率(ETD)
が6GPa以上、より好ましいは7GPa以上である。
この場合、縦方向のヤング率(EMD)は5GPa以上が
好ましい。In the case of a magnetic medium application, the intensity ratio R by the laser Raman scattering method is 6 or more in at least one of the vertical direction and the horizontal direction, and particularly, the intensity ratio R 2 in the horizontal direction is 6 or more.
As described above, it is more preferable to be 7 or more.
Also preferably, the Young's modulus in the transverse direction of the film (E TD )
Is 6 GPa or more, more preferably 7 GPa or more.
In this case, the longitudinal direction of the Young's modulus (E MD) is more 5GPa is preferred.
【0024】特に磁気材料用途の中でもディジタルビデ
オ用途の場合はレーザーラマン散乱法における強度比R
の縦方向と横方向の少なくともいずれか一方が6以上で
あることはもちろんのこと、高いレベルの電磁変換特性
を達成するために少なくとも片側の表面粗さ(Ra)が
0.1nm〜5nmと超平滑な表面であることが好まし
い。In particular, for digital video applications among magnetic materials, the intensity ratio R in the laser Raman scattering method is used.
Of at least one of the vertical direction and the horizontal direction is not less than 6, and in order to achieve a high level of electromagnetic conversion characteristics, the surface roughness (Ra) of at least one side is as large as 0.1 nm to 5 nm. Preferably, the surface is smooth.
【0025】なお、この目的を達するためには少なくと
も2層以上の積層フィルムとし、少なくとも片側の表面
層でこの目的を達成することが好ましい。In order to achieve this object, it is preferable to form a laminated film of at least two layers, and to achieve this object with at least one surface layer.
【0026】熱転写リボン用途の場合は、上記した強度
比Rのうち、少なくとも縦方向の強度比R2 が6以上で
あることがより好ましく、長手方向の、100℃、30
分での熱収縮率が2%以下、さらに1%以下であると、
印字する際のシワがなく、印字むらやインクの過転写を
生じることがなく、高精細な印刷を行うことができる。In the case of a thermal transfer ribbon, at least the strength ratio R 2 in the longitudinal direction among the above-mentioned strength ratios R is more preferably 6 or more.
When the heat shrinkage rate per minute is 2% or less, further 1% or less,
High-definition printing can be performed without wrinkles at the time of printing, without causing printing unevenness and overtransfer of ink.
【0027】コンデンサ用途の場合は、上記した強度比
Rのうち、少なくとも縦方向の強度比R1 が6以上であ
り、かつフィルムの縦方向の破断伸度が100%以下、
さらに好ましくは80%以下とすると、絶縁破壊電圧の
向上と誘電特性の安定化に有効である。In the case of a capacitor application, at least the strength ratio R 1 in the longitudinal direction among the above-mentioned strength ratios R is 6 or more, and the breaking elongation in the longitudinal direction of the film is 100% or less,
More preferably, when it is 80% or less, it is effective for improving the dielectric breakdown voltage and stabilizing the dielectric characteristics.
【0028】感熱孔版原紙用途の場合は、上記した強度
比Rの縦方向と横方向の少なくともいずれか一方が6以
上であり、かつフィルムの融点が230℃以下であり、
及び結晶融解熱(ΔHu)が、50J/g以下である
と、低エネルギーでの穿孔性にも優れ、エネルギーレベ
ルに応じて穿孔径を変化させることが可能であり複数版
でのカラー印刷を行う場合などの印刷性にも優れてい
る。In the case of heat-sensitive stencil paper, at least one of the strength ratio R in the longitudinal direction and the transverse direction is 6 or more, and the melting point of the film is 230 ° C. or less.
When the heat of crystal fusion (ΔHu) is 50 J / g or less, the piercing property at low energy is excellent, the piercing diameter can be changed according to the energy level, and color printing on multiple plates is performed. Excellent printability in some cases.
【0029】本発明で言う同時二軸延伸フィルムとは、
配向付与の方法が同時二軸延伸によって行われるフィル
ムである。本発明の製造方法は、未延伸キャストフィル
ムを、(ポリエステルのガラス転移温度Tg+25)℃
〜(Tg+45)℃の温度範囲で面積延伸倍率2〜7倍
に縦および横方向に同時二軸延伸する第1段目の延伸工
程と、引続き(Tg−15)℃〜(Tg+10)℃の温
度範囲で面積延伸倍率4〜20倍に縦及び横方向に同時
二軸延伸する第2段目の延伸工程を有し、多段階の温度
で多段に同時二軸延伸するものである。The simultaneous biaxially stretched film referred to in the present invention is:
This is a film in which the orientation is imparted by simultaneous biaxial stretching. According to the production method of the present invention, the unstretched cast film is formed by (polyester glass transition temperature Tg + 25) ° C.
The first stretching step of simultaneous biaxial stretching in the vertical and horizontal directions at an area stretching ratio of 2 to 7 times in the temperature range of (Tg + 45) ° C., followed by the temperature of (Tg−15) ° C. to (Tg + 10) ° C. It has a second-stage stretching step of simultaneous biaxial stretching in the vertical and horizontal directions at an area stretching ratio of 4 to 20 times within the range, and performs simultaneous biaxial stretching in multiple stages at multiple temperatures.
【0030】各段階の同時二軸延伸の縦と横の延伸倍率
は、同倍率であってもよく、異なっていてもよい。好ま
しくは、キャストフィルムの両端部を把持具(クリッ
プ)で把持する同時延伸テンターに導き、フィルムを予
熱した後、第1段目と第2段目の同時延伸を行うとき、
縦と横の延伸倍率は同倍率か、もしくは縦と横の延伸倍
率の差を1以下とするのが好ましい。The longitudinal and transverse stretching ratios of the simultaneous biaxial stretching at each stage may be the same or different. Preferably, when the both ends of the cast film are guided to a simultaneous stretching tenter for gripping with a gripper (clip), and after preheating the film, the first and second stages are simultaneously stretched,
It is preferable that the vertical and horizontal stretching ratios are the same, or the difference between the vertical and horizontal stretching ratios is 1 or less.
【0031】未延伸キャストフィルムを、(ポリエステ
ルのガラス転移温度Tg+25)℃〜(Tg+45)℃
の温度範囲で面積延伸倍率2〜7倍に縦および横方向に
同時二軸延伸する第1段目の延伸工程と、引続き(Tg
−15)℃〜(Tg+10)℃の温度範囲で面積延伸倍
率4〜16倍に縦及び横方向に同時二軸延伸する第2段
目の延伸工程と、さらに(ポリエステルの融解温度Tm
−130)℃〜(Tm−10)℃の温度範囲で面積延伸
倍率1.5〜5倍に縦および横方向に同時二軸延伸する
第3段目の延伸工程を有する製造方法によれば、フィル
ムをさらに強力化できる。このとき、第3段目の延伸工
程を多段階の温度で多段に同時二軸延伸するとさらに好
ましい。この場合、第3段目の同時二軸延伸での縦と横
の延伸倍率は、最終二軸延伸フィルムの必要強度特性に
合わせて、縦と横の延伸倍率を本発明の範囲で適宜選択
する。The unstretched cast film is heated at (Tg + 25) ° C. to (Tg + 45) ° C.
A first stretching step of simultaneous biaxial stretching in the longitudinal and transverse directions to an area stretching ratio of 2 to 7 times in a temperature range of
-15) A second stretching step of simultaneously biaxially stretching in the machine and transverse directions at an area stretching ratio of 4 to 16 times in a temperature range of -15 ° C to (Tg + 10) ° C, and further (a melting temperature Tm of the polyester).
According to a production method having a third-stage stretching step of simultaneously biaxially stretching in the vertical and horizontal directions at an area stretching ratio of 1.5 to 5 times in a temperature range of −130) ° C. to (Tm−10) ° C. The film can be further strengthened. At this time, it is more preferable that the third-stage stretching step be performed simultaneously and biaxially in multiple stages at multiple temperatures. In this case, the longitudinal and transverse stretching ratios in the third-stage simultaneous biaxial stretching are appropriately selected according to the required strength characteristics of the final biaxially stretched film within the scope of the present invention. .
【0032】同時二軸延伸後、(ポリエステルの融解温
度Tm−60)℃〜(Tm−10)℃の温度範囲で熱固
定を行い、熱固定温度からの冷却過程で縦および横方向
に弛緩処理を行うことが熱寸法安定性の点で好ましい。
ここで面積延伸倍率とは、縦延伸倍率と横延伸倍率の積
である。After simultaneous biaxial stretching, heat setting is performed in the temperature range of (polyester melting temperature Tm−60) ° C. to (Tm−10) ° C., and relaxation treatment in the longitudinal and horizontal directions is performed during the cooling process from the heat setting temperature. Is preferred in terms of thermal dimensional stability.
Here, the area stretch ratio is a product of the longitudinal stretch ratio and the transverse stretch ratio.
【0033】本発明の同時二軸延伸において、フィルム
端部の把持具(クリップ)の温度は(ポリエステルのガ
ラス転移温度Tg+15)℃〜(Tg+50)℃の温度
範囲が好ましく、またフィルム端部と把持具とが接触す
る面の形状において、長手方向の長さ(LMD)と幅方向
の長さ(LTD)の比(LMD/LTD)を3〜15の範囲と
する把持部を有するクリップを用いて同時二軸延伸する
ことが、クリップ把持部分のフィルムの延伸倍率を高め
る点で好ましい。In the simultaneous biaxial stretching of the present invention, the temperature of the gripper (clip) at the end of the film is preferably in the temperature range of (glass transition temperature of polyester Tg + 15) ° C. to (Tg + 50) ° C. In the shape of the surface that comes into contact with the tool, it has a gripping part having a ratio (L MD / L TD ) of the length in the longitudinal direction (L MD ) to the length in the width direction (L TD ) in the range of 3 to 15. Simultaneous biaxial stretching using a clip is preferred from the viewpoint of increasing the stretching ratio of the film at the clip holding portion.
【0034】ここで把持具(クリップ)の温度とは、把
持具はテンター中の延伸、熱固定ゾーンの熱風で加熱さ
れつつ通過しテンターから排出され、オーブンの外周を
リターンしてテンター入口に導かれるが、このとき、フ
ィルム端部を把持する前の把持具(クリップ)の温度を
言う。把持具の温度は、外周をリターンする工程で、冷
却のための冷風の風量、冷却部の長さを制御して行う。
この温度は製膜条件に設定して3〜5時間の連続運転で
定常温度になる。Here, the temperature of the gripper (clip) means that the gripper passes through the tenter while being heated by the hot air in the stretching and heat fixing zone, is discharged from the tenter, returns to the outer periphery of the oven, and is guided to the tenter inlet. At this time, it refers to the temperature of the gripper (clip) before gripping the edge of the film. The temperature of the gripper is controlled by controlling the amount of cold air for cooling and the length of the cooling unit in the step of returning to the outer periphery.
This temperature is set to a film forming condition and becomes a steady temperature in a continuous operation for 3 to 5 hours.
【0035】また、フィルム端部と把持具とが接触する
面の形状とは、紙の間にカーボン紙を挟み込んだ状態、
あるいは加圧発色する感圧フィルムを把持具に挟み込ん
で、加圧印画したときに得られる形状を言う。本発明で
は、この形状の縦方向の長さ(LMD)は、15〜30m
mが好ましい。Further, the shape of the surface where the film end and the gripping tool come into contact with each other is such that the carbon paper is sandwiched between the papers,
Alternatively, it refers to a shape obtained when a pressure-sensitive film that develops color under pressure is sandwiched between grippers and subjected to pressure printing. In the present invention, the longitudinal length of the shape (L MD) is, 15 to 30 m
m is preferred.
【0036】また、本発明の同時二軸延伸では、第1段
目の温度を(ポリエステルのガラス転移温度Tg+2
5)℃〜(Tg+45)℃の温度範囲とし、第2段目の
温度を(Tg−15)℃〜(Tg+10)℃の温度範囲
で行うことで、フィルムの端部部分の延伸性を高め、か
つ第2段目の同時二軸延伸後のフィルム中央部の強度を
高める効果があり、さらに第3段目以降の同時二軸延伸
性が良くなり、同時二軸延伸後のフィルムの強度をさら
に高めることができる。In the simultaneous biaxial stretching of the present invention, the temperature of the first stage is set to (the glass transition temperature Tg + 2 of the polyester).
5) The temperature range of ° C to (Tg + 45) ° C, and the second stage temperature is performed in the temperature range of (Tg-15) ° C to (Tg + 10) ° C, thereby improving the stretchability of the end portion of the film. In addition, there is an effect of increasing the strength of the central portion of the film after the simultaneous biaxial stretching of the second stage, and the simultaneous biaxial stretchability of the third and subsequent stages is improved, and the strength of the film after the simultaneous biaxial stretching is further increased. Can be enhanced.
【0037】なお、本発明において未延伸キャストフィ
ルムとは、十分乾燥された原料ペレットを押出機に供給
し、T型等の口金により、回転する金属製キャスティン
グドラム上にシート状に押し出し、冷却固化せしめたも
の、もしくは未乾燥ペレットをベント式押出機に供給し
同様にして得られたものをいう。In the present invention, the unstretched cast film refers to a sufficiently dried raw material pellet supplied to an extruder, extruded into a sheet on a rotating metal casting drum by means of a die such as a T-shape, and cooled and solidified. It refers to a crushed pellet or a pellet obtained by supplying undried pellets to a vented extruder.
【0038】次に、本発明の二軸延伸ポリエステルフィ
ルムの製造法の具体的な例について説明するが、本発明
方法はかかる例に限定されるものではない。Next, specific examples of the method for producing the biaxially stretched polyester film of the present invention will be described, but the present invention is not limited to such examples.
【0039】ポリエステルとして、ポリエチレンテレフ
タレートのペレットを真空下で十分に乾燥して、270
〜300℃の温度に加熱された押出機に供給し、T型口
金よりシート状に押し出す。この溶融されたシートを、
表面温度10〜40℃に冷却されたドラム上に静電気力
で密着させて冷却固化し、実質的に非晶状態の未延伸キ
ャストフィルムを得る。このキャストフィルムを、フィ
ルム両端部を走行するクリップで把持して同時二軸延伸
テンターに導き、予熱ゾーンで100〜120℃に加熱
し、縦および横の延伸倍率を1.5〜2.5倍の範囲
で、面積延伸倍率を2〜7倍の範囲に第1段目の同時二
軸延伸を行う。このとき、フィルム端部を把持するクリ
ップの温度は、90〜130℃の温度範囲にするのが好
ましい。引続き、60〜85℃の温度に降温し、縦およ
び横の延伸倍率を2〜5倍の範囲で、面積延伸倍率を4
〜20倍の範囲に第2段目の同時二軸延伸を行う。ある
いは、第2段目の同時二軸延伸の面積延伸倍率を4〜1
6倍の範囲で行い、引続き、125〜245℃、好まし
くは130〜210℃の温度範囲で、縦および横の延伸
倍率を1.0〜2.5倍の範囲で、面積延伸倍率を1.
5〜5倍の範囲に第3段目の同時二軸延伸を行う。第3
段目の同時二軸延伸は、2段階以上の温度で多段階に分
割して行うことが好ましい。例えば、125〜160℃
の温度範囲と161〜245℃の温度範囲で延伸倍率を
分割して同時二軸延伸を行うことが強度発現の点で好ま
しい。As a polyester, polyethylene terephthalate pellets were sufficiently dried under vacuum to
It is supplied to an extruder heated to a temperature of about 300 ° C. and extruded from a T-type die into a sheet. This melted sheet is
It is brought into close contact with a drum cooled to a surface temperature of 10 to 40 ° C. by electrostatic force and solidified by cooling to obtain a substantially amorphous unstretched cast film. This cast film is gripped by clips running on both ends of the film, guided to a simultaneous biaxial stretching tenter, heated to 100 to 120 ° C. in a preheating zone, and stretched vertically and horizontally at a magnification of 1.5 to 2.5 times. , The first-stage simultaneous biaxial stretching is performed in an area stretching ratio of 2 to 7 times. At this time, it is preferable that the temperature of the clip that grips the end of the film be in a temperature range of 90 to 130 ° C. Subsequently, the temperature was lowered to a temperature of 60 to 85 ° C., the vertical and horizontal stretching ratios were in the range of 2 to 5 times, and the area stretching ratio was 4
The second-stage simultaneous biaxial stretching is performed in a range of up to 20 times. Alternatively, the area stretching ratio of the second-stage simultaneous biaxial stretching is 4 to 1
The stretching is performed in a range of 6 times, and subsequently, in a temperature range of 125 to 245 ° C., preferably 130 to 210 ° C., a longitudinal and transverse stretching ratio is in a range of 1.0 to 2.5 times, and an area stretching ratio is 1.
The third-stage simultaneous biaxial stretching is performed in a range of 5 to 5 times. Third
It is preferable that the simultaneous biaxial stretching of the stage is performed in multiple stages at two or more stages of temperature. For example, 125-160 ° C
It is preferable from the viewpoint of strength development that the stretching ratio is divided in the temperature range of 161 to 245 ° C. and the simultaneous biaxial stretching is performed.
【0040】こうして二軸延伸されたフィルムに平面
性、寸法安定性を付与するために、195〜245℃の
温度範囲で熱固定を行い、熱固定温度からの冷却過程
で、好ましくは100〜200℃の温度範囲で縦および
横方向に、好ましくは1〜6%の範囲で弛緩処理を行
う。その処理後、フィルムを室温まで冷やして巻き取
り、目的とするレーザーラマン散乱法で測定した161
5cm-1における縦方向のピーク強度(IMD)と厚み方
向のピーク強度(IND)との比R1 (=IMD/IND)と
横方向のピーク強度(ITD)と厚み方向のピーク強度
(IND)との比R2 (=ITD/IND)の少なくともいず
れか一方が6以上の同時二軸延伸ポリエステルフィルム
を得る。In order to impart flatness and dimensional stability to the film thus biaxially stretched, the film is heat-set at a temperature in the range of 195 to 245 ° C. The relaxation treatment is carried out in the vertical and horizontal directions in a temperature range of ° C., preferably in the range of 1 to 6%. After the treatment, the film was cooled to room temperature, wound up, and measured by a target laser Raman scattering method.
The ratio R 1 (= I MD / I ND ) between the peak intensity in the vertical direction ( IMD ) and the peak intensity in the thickness direction (I ND ) at 5 cm −1, the peak intensity in the horizontal direction (I TD ) and the thickness in the thickness direction A simultaneously biaxially stretched polyester film having a ratio R 2 (= I TD / I ND ) to the peak intensity (I ND ) of 6 or more is obtained.
【0041】なお、本発明では、フィルムの表面特性を
付与するため、例えば易接着性、易滑性、離型性、制電
性を付与するために、フィルムの同時二軸延伸の前また
は後の工程で、ポリエステルフィルムの表面に塗材をコ
ーティングすることができる。In the present invention, before or after simultaneous biaxial stretching of the film, in order to impart surface properties of the film, for example, to impart easy adhesion, easy slipping, releasing property, and antistatic property. In the step, the surface of the polyester film can be coated with a coating material.
【0042】[物性値の測定、評価法] (1)ガラス転移温度Tg、融解温度Tm、結晶融解熱
ΔHu 示差走査熱量計として、セイコー電子工業(株)製“ロ
ボットDSC−RDC220”を用い、データー解析装
置として、同社製“ディスクセッション”SSC/52
00を用い、サンプルを約5mg採取し、室温から昇温
速度20℃/分で300℃まで加熱した時に得られる熱
カーブより、Tg、Tmを求める。また、融解に伴う融
解吸熱カーブの面積から結晶融解熱ΔHuを求める。[Measurement and Evaluation Methods for Physical Properties] (1) Glass transition temperature Tg, melting temperature Tm, heat of crystal melting ΔHu As a differential scanning calorimeter, “Robot DSC-RDC220” manufactured by Seiko Instruments Inc. is used. As a data analysis device, the company's “Disk Session” SSC / 52
Using T.00, about 5 mg of a sample is collected, and Tg and Tm are determined from a heat curve obtained when the sample is heated from room temperature to 300 ° C. at a rate of temperature increase of 20 ° C./min. Further, the heat of crystal fusion ΔHu is determined from the area of the melting endothermic curve accompanying the melting.
【0043】(2)レーザーラマン散乱法によるフィル
ムの配向 レーザーラマン分光の測定条件は次のとおりである。 装 置 :Jobin Yvon社製 Ramanor U-1000 マイクロラマン:測定配置 180°散乱 試料台 固体 光 源 :Ar+ レーザー、NEC GLG3300 、波長515nm 分光器 :構成 1m Czerny-Turner 型 Double Monochromator 回折格子 Plane Holographic、1800g/mm、 110×110mm 分散 9.23cm-1/mm 逆光除去率 10-14 (20cm-1) 検出器 :PM RCA31034、浜松電子製943−02 測定に用いたフィルムはポリメチルメタクリレートに包
埋後、湿式研磨し、断面は横方向に平行にした。測定部
分は中心部分とし、位置を少しずらして10回測定し平
均値をとった。測定は縦方向に平行な偏光測定における
1615cm-1バンドの強度(IMD)と厚み方向に平行
な偏光測定における1615cm-1バンドの強度
(IND)をとり、配向を表す比RをR1 =IMD/INDと
した。また横方向に平行な偏光測定における1615c
m-1バンドの強度(ITD)と厚み方向に平行な偏光測定
における1615cm-1バンドの強度(IND)をとり、
配向を表す比RをR2 =ITD/INDとした。(2) Orientation of Film by Laser Raman Scattering The measurement conditions of laser Raman spectroscopy are as follows. Apparatus: Ramanor U-1000 manufactured by Jobin Yvon Micro Raman: Measurement arrangement 180 ° scattering Sample stand Solid light source: Ar + laser, NEC GLG3300, wavelength 515 nm Spectrometer: Configuration 1 m Czerny-Turner type double monochromator diffraction grating 1800 g / mm, 110 × 110 mm Dispersion 9.23 cm −1 / mm Backlight removal rate 10 −14 (20 cm −1 ) Detector: PM RCA31034, 943-02 manufactured by Hamamatsu Electronics The film used for measurement is embedded in polymethyl methacrylate. Thereafter, wet polishing was performed to make the cross section parallel to the lateral direction. The measurement part was the center part, the position was slightly shifted, and the measurement was performed ten times to obtain an average value. The measurement takes the intensity (I MD ) of the 1615 cm −1 band in the polarization measurement parallel to the longitudinal direction and the intensity (I ND ) of the 1615 cm −1 band in the polarization measurement parallel to the thickness direction, and sets the ratio R representing the orientation to R 1. = I MD / IND . 1615c in polarization measurement parallel to the horizontal direction
m -1 band intensity (I TD) and the intensity of the 1615 cm -1 band in parallel polarization measurements in the thickness direction (I ND) take,
The ratio R representing the orientation was R 2 = ITD / IND .
【0044】(3)高速削れ性 フィルムを幅1/2 インチのテープ状にスリットしたもの
をテープ走行性試験機を使用して、ガイドピン(表面粗
度:Raで100nm)上を走行させる(走行速度25
0m/分、走行回数1パス、巻き付け角:60゜、走行
張力:90g)。このとき、フィルムを走行させ終わっ
た後のガイドピンを肉眼で観察し、白粉の付着が見られ
ないものを優(○)、白粉の付着が若干見られるものを
良(△)、白粉が多く付着しているものは不良(×)と
判定した。優が望ましいが、良でも実用的には使用可能
である。(3) High-speed scraping property A film obtained by slitting a film into a tape having a width of 1/2 inch is run on guide pins (surface roughness: 100 nm in Ra) using a tape running tester ( Travel speed 25
0 m / min, running frequency 1 pass, winding angle: 60 °, running tension: 90 g). At this time, the guide pins after running the film were visually observed, and those with no white powder adhesion were excellent (○), those with some white powder adhesion good (△), and many white powders Those that were attached were judged to be defective (x). Although excellent is desirable, even good is practically usable.
【0045】(4)ヤング率 オリエンテック(株)製フィルム強伸度自動測定装置
“テンシロンAMF/RTA−100”を用いて、試料
フィルムを幅10mm、試長間100mm、引張り速度
200mm/分で引っ張った。得られた張力−歪曲線の
立上がりの接線の勾配からヤング率を求めた。測定は2
5℃、65%RHの雰囲気下で行った。(4) Young's modulus Using an automatic film strength and elongation measuring device “Tensilon AMF / RTA-100” manufactured by Orientec Co., Ltd., a sample film was prepared at a width of 10 mm, a test length of 100 mm, and a pulling speed of 200 mm / min. I pulled. The Young's modulus was determined from the slope of the rising tangent of the obtained tension-strain curve. Measurement is 2
The test was performed in an atmosphere of 5 ° C. and 65% RH.
【0046】(5)破れ頻度 真空乾燥したポリエチレンテレフタレートをT型口金か
ら、静電気力でキャスティングドラム上に密着させて冷
却固化せしめて、キャストフィルムを得、複数のロール
からなる長手方向延伸装置、あるいはテンターによる延
伸、熱固定装置での延伸に伴うフィルム破れを観察し
て、次の基準で判定した。 ◎:エッジからの破れが皆無である場合 ○:エッジからの破れが極まれに生じる場合 △:エッジからの破れが時々生じる場合 ×:エッジからの破れが頻発する場合(5) Breakage frequency Vacuum-dried polyethylene terephthalate is brought into close contact with the casting drum by electrostatic force from a T-type die and solidified by cooling to obtain a cast film, and a longitudinal stretching device comprising a plurality of rolls, or Observation of stretching by a tenter and tearing of the film due to stretching by a heat setting device was made and judged according to the following criteria. ◎: When there is no tear from the edge ○: When the tear from the edge occurs very rarely Δ: When the tear from the edge occurs occasionally ×: When the tear from the edge occurs frequently
【0047】(6)電磁変換特性(C/N) 本発明のフィルムの表面に、下記組成の磁性塗料および
非磁性塗料をエクストルージョンコーターにより重層塗
布(上層は磁性塗料で塗布厚0.1μm、非磁性下層の
厚みは適宜変化させた)し、磁気配向させ、乾燥させ
る。次いで反対面に下記組成のバックコート層を形成し
た後、小型テストカレンダー装置(スチール/スチール
ロール、5段)で、温度:85℃、線圧:200kg/
cmでカレンダー処理した後、60℃で、48時間キュ
アリングする。上記テープ原反を8mm幅にスリット
し、パンケーキを作成した。次いで、このパンケーキか
ら長さ200m分を、カセットに組み込んでカセットテ
ープとした。このテープに、市販のHi8用VTR(S
ONY社製 EV−BS3000)を用いて、7MHz
+1MHzのC/N(キャリア対ノイズ比)の測定を行
った。(6) Electromagnetic conversion characteristics (C / N) A magnetic paint and a non-magnetic paint having the following compositions are applied on the surface of the film of the present invention by an extrusion coater. The thickness of the non-magnetic lower layer was appropriately changed), magnetically oriented, and dried. Next, after forming a back coat layer having the following composition on the opposite surface, a small test calender (steel / steel roll, 5 steps) was used to obtain a temperature of 85 ° C. and a linear pressure of 200 kg /.
After calendering at 60 ° C., cure at 60 ° C. for 48 hours. The raw tape was slit into a width of 8 mm to prepare a pancake. Next, a 200 m length of this pancake was incorporated into a cassette to form a cassette tape. This tape has a commercially available Hi8 VTR (S
7MHz using ONY EV-BS3000)
A +1 MHz C / N (carrier to noise ratio) measurement was performed.
【0048】 (磁性塗料の組成) ・強磁性金属粉末 : 100重量部 ・スルホン酸Na変成塩化ビニル共重合体 : 10重量部 ・スルホン酸Na変成ポリウレタン : 10重量部 ・ポリイソシアネート : 5重量部 ・ステアリン酸 : 1.5重量部 ・オレイン酸 : 1重量部 ・カーボンブラック : 1重量部 ・アルミナ : 10重量部 ・メチルエチルケトン : 75重量部 ・シクロヘキサノン : 75重量部 ・トルエン : 75重量部 (非磁性下層塗料の組成) ・酸化チタン : 100重量部 ・カーボンブラック : 10重量部 ・スルホン酸Na変成塩化ビニル共重合体 : 10重量部 ・スルホン酸Na変成ポリウレタン : 10重量部 ・メチルエチルケトン : 30重量部 ・メチルイソブチルケトン : 30重量部 ・トルエン : 30重量部 (バックコートの組成) ・カーボンブラック(平均粒径20nm) : 95重量部 ・カーボンブラック(平均粒径280nm): 10重量部 ・αアルミナ : 0.1重量部 ・酸化亜鉛 : 0.3重量部 ・スルホン酸Na変成ポリウレタン : 20重量部 ・スルホン酸Na変成塩化ビニル共重合体 : 30重量部 ・シクロヘキサノン : 200重量部 ・メチルエチルケトン : 300重量部 ・トルエン : 100重量部(Composition of magnetic paint) ・ Ferromagnetic metal powder: 100 parts by weight ・ Na sulfonate-modified vinyl chloride copolymer: 10 parts by weight ・ Na sulfonate-modified polyurethane: 10 parts by weight ・ Polyisocyanate: 5 parts by weight ・Stearic acid: 1.5 parts by weight-Oleic acid: 1 part by weight-Carbon black: 1 part by weight-Alumina: 10 parts by weight-Methyl ethyl ketone: 75 parts by weight-Cyclohexanone: 75 parts by weight-Toluene: 75 parts by weight (nonmagnetic lower layer) Composition of paint) ・ Titanium oxide: 100 parts by weight ・ Carbon black: 10 parts by weight ・ Na sulfonate-modified vinyl chloride copolymer: 10 parts by weight ・ Na sulfonate-modified polyurethane: 10 parts by weight ・ Methyl ethyl ketone: 30 parts by weight ・ Methyl Isobutyl ketone: 30 parts by weight ・ Toluene: 30 layers Part (composition of back coat) ・ Carbon black (average particle diameter 20 nm): 95 parts by weight ・ Carbon black (average particle diameter 280 nm): 10 parts by weight ・ α-alumina: 0.1 part by weight ・ Zinc oxide: 0.3 part by weight Parts-Na sulfonate-modified polyurethane: 20 parts by weight-Na sulfonate-modified vinyl chloride copolymer: 30 parts by weight-Cyclohexanone: 200 parts by weight-Methyl ethyl ketone: 300 parts by weight-Toluene: 100 parts by weight
【0049】(7)印字むらおよび階調性評価 得られたフィルムにシアン、マゼンタ、イエローのイン
キ層を塗布してプリンタリボンを作成し、バリアブルド
ット方式の熱転写型カラープリンタで色彩パターンの標
準印刷をし、目視で階調性を評価した。また、印刷部分
の均一性によりリボンにシワが入っていないかどうかを
併せて目視で判定した。(7) Evaluation of print unevenness and gradation property A cyan, magenta, and yellow ink layer is applied to the obtained film to form a printer ribbon, and standard printing of a color pattern is performed using a variable dot thermal transfer color printer. Then, the gradation was visually evaluated. In addition, it was also visually determined whether or not the ribbon had wrinkles due to the uniformity of the printed portion.
【0050】(8)コンデンサ用特性評価 A.誘電特性 フィルムの両面に直径18mmの円状にアルミニウムを
600〜1000オングストロームの厚さになるように
蒸着したものを試験片とし、試験片はあらかじめ温度2
0±5℃、相対湿度65±5%の雰囲気に48時間以上
放置しておく。TA Instruments社の誘電
特性測定装置DEA−2970を用いて、周波数1kH
z、昇温速度2℃/分で誘電正接の温度依存性を測定
し、105℃における誘電正接の値が1.3%以下のも
のを合格とした。(8) Evaluation of Characteristics for Capacitor Dielectric properties A test piece was prepared by depositing aluminum on both sides of a film in a circular shape having a diameter of 18 mm so as to have a thickness of 600 to 1000 angstroms.
Leave for 48 hours or more in an atmosphere of 0 ± 5 ° C. and 65 ± 5% relative humidity. A frequency of 1 kHz was measured using a dielectric property measuring device DEA-2970 manufactured by TA Instruments.
z, the temperature dependence of the dielectric loss tangent was measured at a heating rate of 2 ° C./min, and those having a dielectric loss tangent at 105 ° C. of 1.3% or less were accepted.
【0051】B.絶縁破壊電圧 JIS−C−2319に記載の方法に準じて、ただし、
金属蒸着を施していないフィルムを試験片として用いて
次のように評価する。適当な大きさの金属製平板の上に
ゴムショア硬さ約60度、厚さ約2mmのゴム板を一枚
敷き、その上に厚さ約6μmのアルミニウム箔を10枚
重ねたものを下部電極とし、約50gの重さで周辺に約
1mmの丸みを持った径8mmの底面が平滑で傷のない
黄銅製円柱を上部電極とする。試験片はあらかじめ温度
20±5℃、相対湿度65±5%の雰囲気に48時間以
上放置しておく。上部電極と下部電極の間に試験片をは
さみこみ、温度20±5℃、相対湿度65±5%の雰囲
気中で両電極間に直流電源により直流電圧を印加し、該
直流電圧を1秒間に100Vの速さで0Vから絶縁破壊
するまで上昇させる。試料50個に対し試験を行い、絶
縁破壊電圧を試験片の厚みで除したものの平均値を求
め、その値が400V/μm以上を合格とする。B. Dielectric breakdown voltage According to the method described in JIS-C-2319, except that
Using a film without metal deposition as a test piece, evaluation is made as follows. A rubber plate having a rubber shore hardness of about 60 degrees and a thickness of about 2 mm is laid on a metal plate of an appropriate size, and 10 aluminum foils of about 6 μm thickness are laid on the rubber plate as a lower electrode. The upper electrode is a brass cylinder having a weight of about 50 g, a round bottom of about 1 mm, a diameter of about 8 mm, a smooth bottom surface and no damage. The test piece is previously left in an atmosphere at a temperature of 20 ± 5 ° C. and a relative humidity of 65 ± 5% for 48 hours or more. A test piece is sandwiched between the upper electrode and the lower electrode, and a DC voltage is applied between both electrodes by a DC power supply in an atmosphere at a temperature of 20 ± 5 ° C. and a relative humidity of 65 ± 5%. At 0 V until the dielectric breakdown occurs. A test is performed on 50 samples, and an average value obtained by dividing the dielectric breakdown voltage by the thickness of the test piece is determined. A value of 400 V / μm or more is regarded as a pass.
【0052】[0052]
【実施例】以下に、本発明のより具体的な実施例につい
て説明する。 実施例1、2、比較例1、2 ポリエチレンテレフタレート(固有粘度0.65、ガラ
ス転移温度75℃、融点255℃、平均径0.3μmの
球状架橋ポリスチレン粒子0.1重量%配合)のペレッ
トを180℃で3時間真空乾燥した後に、280℃に加
熱された押出機に供給して溶融押出し、Tダイよりシー
ト状に吐出した。さらにこのシートを表面温度25℃の
冷却ドラム上に静電気力で密着させて冷却固化し、未延
伸キャストフィルムを得た。この未延伸フィルムの両端
部をクリップで把持して、クリップをリニアモータ方式
で駆動する駆動装置を具備した同時二軸延伸テンターに
導き、110℃の温度で予熱し、表1に示した延伸倍率
で第1段目の同時二軸延伸を行い、引続き80℃の温度
で、表1に示した延伸倍率で第二段目の同時二軸延伸を
行った後、さらに、210℃の温度で熱固定を施した
後、120℃の冷却ゾーンで縦方向に1.5%、横方向
に2%の弛緩率で弛緩処理を行い、フィルムを室温に徐
冷して巻き取った。フィルム厚みは押出量を調節して9
μmに合わせた。この時のクリップ温度は100℃とし
た。比較例では、同時二軸延伸を表1に示す延伸温度、
倍率とした以外は実施例1と同様に行った。フィルム端
部のクリップ把持跡を観察すると、実施例1、2ではフ
ィルムの延伸跡が見られたが、比較例1、2では、フィ
ルムに把持跡の未延伸部分が見られ、フィルム端部から
のフィルム破れが見られる。フィルムの製造条件(延伸
温度、倍率)を表1に、得られたフィルムのレーザーラ
マン散乱法で得たピーク強度比R、ヤング率、破れ頻度
を表2に示した。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, more specific embodiments of the present invention will be described. Examples 1 and 2 and Comparative Examples 1 and 2 A pellet of polyethylene terephthalate (containing 0.1% by weight of spherical crosslinked polystyrene particles having an intrinsic viscosity of 0.65, a glass transition temperature of 75 ° C, a melting point of 255 ° C, and an average diameter of 0.3 µm) was prepared. After vacuum drying at 180 ° C. for 3 hours, the mixture was supplied to an extruder heated to 280 ° C., melt-extruded, and discharged from a T-die into a sheet. Further, this sheet was brought into close contact with a cooling drum having a surface temperature of 25 ° C. by electrostatic force and cooled and solidified to obtain an unstretched cast film. Both ends of the unstretched film are gripped with clips, guided to a simultaneous biaxial stretching tenter equipped with a drive device for driving the clips by a linear motor, preheated at a temperature of 110 ° C., and stretched as shown in Table 1. Then, the first-stage simultaneous biaxial stretching was performed, and then the second-stage simultaneous biaxial stretching was performed at a temperature of 80 ° C. and at the stretching ratio shown in Table 1, and then heated at a temperature of 210 ° C. After fixing, the film was subjected to a relaxation treatment in a cooling zone at 120 ° C. at a relaxation rate of 1.5% in the longitudinal direction and 2% in the lateral direction, and the film was gradually cooled to room temperature and wound up. The film thickness is adjusted to 9
It was adjusted to μm. The clip temperature at this time was 100 ° C. In the comparative example, the simultaneous biaxial stretching was performed at the stretching temperature shown in Table 1,
The procedure was performed in the same manner as in Example 1 except that the magnification was changed. When observing the clip grip trace of the film end, in Examples 1 and 2, a stretched trace of the film was seen, but in Comparative Examples 1 and 2, an unstretched portion of the grip trace was seen in the film, and from the film end. The film is broken. Table 1 shows the film production conditions (stretching temperature, magnification), and Table 2 shows the peak intensity ratio R, Young's modulus, and tear frequency of the obtained film obtained by the laser Raman scattering method.
【0053】[0053]
【表1】 [Table 1]
【0054】[0054]
【表2】 [Table 2]
【0055】実施例3、4、比較例3、4 ポリエチレンテレフタレート(固有粘度0.65、ガラ
ス転移温度75℃、融点255℃、平均径0.3μmの
球状架橋ポリスチレン粒子0.1重量%配合)のペレッ
トを180℃で3時間真空乾燥した後に、280℃に加
熱された押出機に供給して溶融押出し、Tダイよりシー
ト状に吐出した。さらにこのシートを表面温度25℃の
冷却ドラム上に静電気力で密着させて冷却固化し、未延
伸キャストフィルムを得た。この未延伸フィルムの両端
部をクリップで把持して、クリップをリニアモータ方式
で駆動する駆動装置を具備した同時二軸延伸テンターに
導き、110℃の温度で予熱し、表3に示した延伸倍率
で第1段目の同時二軸延伸を行い、引続き80℃の温度
で、表3に示した延伸倍率で第二段目の同時二軸延伸を
行った。引続き、160℃の温度で表3に示す延伸倍率
で第3段目の同時二軸延伸を行った。210℃の温度で
熱固定を施した後、120℃の冷却ゾーンで縦方向に2
%、横方向に3%の弛緩率で弛緩処理を行い、フィルム
を室温に徐冷して巻取った。フィルム厚みは押出量を調
節して9μmに合わせた。この時のクリップ温度は10
5℃とした。比較例として、同時二軸延伸を表3に示す
延伸温度、倍率とした以外は実施例と同様ににした。フ
ィルム端部のクリップ把持跡を観察すると、実施例3、
4ではフィルムの把持部がほぼ縦方向の延伸倍率まで延
伸しており、比較例3は、フィルムの把持部は延伸倍率
の低い部分が見られ、フィルム端部からのフィルム破れ
が見られる。また比較例4はフィルム端部からのフィル
ム破れがあり、延伸ができなかった。フィルムの製造条
件(延伸温度、倍率)を表3に、得られたフィルムのレ
ーザーラマン散乱法で得たピーク強度比R、ヤング率、
破れ頻度を表4に示した。Examples 3 and 4, Comparative Examples 3 and 4 Polyethylene terephthalate (containing 0.1% by weight of spherical crosslinked polystyrene particles having an intrinsic viscosity of 0.65, a glass transition temperature of 75 ° C., a melting point of 255 ° C. and an average diameter of 0.3 μm) After vacuum drying the pellets at 180 ° C. for 3 hours, the pellets were supplied to an extruder heated to 280 ° C., melt-extruded, and discharged from a T-die into a sheet. Further, this sheet was brought into close contact with a cooling drum having a surface temperature of 25 ° C. by electrostatic force and cooled and solidified to obtain an unstretched cast film. Both ends of the unstretched film are gripped by clips and guided to a simultaneous biaxial stretching tenter equipped with a drive device for driving the clips by a linear motor system, preheated at a temperature of 110 ° C., and stretched as shown in Table 3. , The first-stage simultaneous biaxial stretching was performed, and subsequently, the second-stage simultaneous biaxial stretching was performed at a temperature of 80 ° C. and a stretching ratio shown in Table 3. Subsequently, the third-stage simultaneous biaxial stretching was performed at a temperature of 160 ° C. and a stretching ratio shown in Table 3. After heat-setting at a temperature of 210 ° C., a vertical cooling in a cooling zone of 120 ° C.
% And a relaxation rate of 3% in the transverse direction, and the film was gradually cooled to room temperature and wound up. The film thickness was adjusted to 9 μm by adjusting the extrusion amount. The clip temperature at this time is 10
5 ° C. As a comparative example, the procedure was the same as in the example, except that the simultaneous biaxial stretching was performed at the stretching temperature and magnification shown in Table 3. When observing the gripping trace of the clip at the end of the film, Example 3,
In No. 4, the grip portion of the film is stretched to almost the stretching ratio in the vertical direction, and in Comparative Example 3, a portion of the grip portion of the film having a low stretch ratio is seen, and the film is torn from the edge of the film. In Comparative Example 4, the film was torn from the edge of the film, and could not be stretched. Table 3 shows the film production conditions (stretching temperature, magnification), and the peak intensity ratio R, Young's modulus, and the like of the obtained film obtained by the laser Raman scattering method.
Table 4 shows the breaking frequency.
【0056】比較例5 ポリエチレンテレフタレート(固有粘度0.65、ガラ
ス転移温度75℃、融点255℃、平均径0.3μmの
球状架橋ポリスチレン粒子0.1重量%配合)のペレッ
トを180℃で3時間真空乾燥した後に、280℃に加
熱された押出機に供給して溶融押出し、Tダイよりシー
ト状に吐出した。さらにこのシートを表面温度25℃の
冷却ドラム上に静電気力で密着させて冷却固化し、未延
伸キャストフィルムを得た。この未延伸キャストフィル
ムを加熱金属ロール群に導き、90℃の温度に加熱し
て、縦方向に3.1倍の延伸倍率で延伸し、この縦延伸
フィルムをテンターに導き、フィルム端部をクリップで
把持し、95℃の温度に加熱して横方向に3.3倍の延
伸倍率で延伸した。この二軸延伸フィルムを加熱金属ロ
ール群に導き、160℃の温度に加熱して、縦方向に
1.3倍の延伸倍率で再延伸した。この延伸フィルムを
テンターに導き、フィルム端部をクリップで把持して、
200℃の温度に加熱して横方向に1.2倍の倍率で延
伸し、引続き210℃の温度で熱固定して室温まで徐冷
して巻取った。フィルム厚みは押出量を調節して9μm
に合わせた。得られたフィルムのレーザーラマン散乱法
で得たピーク強度比R、ヤング率、破れ頻度を表4に示
した。Comparative Example 5 Pellets of polyethylene terephthalate (containing 0.1% by weight of spherical crosslinked polystyrene particles having an intrinsic viscosity of 0.65, a glass transition temperature of 75 ° C., a melting point of 255 ° C. and an average diameter of 0.3 μm) were mixed at 180 ° C. for 3 hours. After vacuum drying, it was supplied to an extruder heated to 280 ° C., melt-extruded, and discharged from a T-die into a sheet. Further, this sheet was brought into close contact with a cooling drum having a surface temperature of 25 ° C. by electrostatic force and cooled and solidified to obtain an unstretched cast film. The unstretched cast film is guided to a group of heated metal rolls, heated to a temperature of 90 ° C., stretched in the longitudinal direction at a stretch ratio of 3.1 times, and the longitudinally stretched film is guided to a tenter. , And heated to a temperature of 95 ° C. and stretched in the transverse direction at a stretch ratio of 3.3 times. The biaxially stretched film was guided to a group of heated metal rolls, heated to a temperature of 160 ° C., and stretched in the longitudinal direction again at a stretch ratio of 1.3 times. Guide this stretched film to a tenter, grip the film end with a clip,
The film was heated at a temperature of 200 ° C., stretched in a transverse direction at a magnification of 1.2 times, then heat-set at a temperature of 210 ° C., gradually cooled to room temperature, and wound. The film thickness is 9μm by adjusting the extrusion amount
I adjusted to. Table 4 shows the peak intensity ratio R, Young's modulus, and breaking frequency of the obtained film obtained by the laser Raman scattering method.
【0057】[0057]
【表3】 [Table 3]
【0058】[0058]
【表4】 [Table 4]
【0059】実施例5 押出機A,B2台を用い、280℃に加熱された押出機
AにはポリエチレンテレフタレートI(固有粘度0.6
5、ガラス転移温度75℃、融点255℃、平均径0.
2μmの球状架橋ポリスチレン0.2重量%配合)のペ
レットを180℃で3時間真空乾燥した後に供給し、同
じく280℃に加熱された押出機Bには、ポリエチレン
テレフタレートII(固有粘度0.65、ガラス転移温度
75℃、融点255℃、平均径0.3μmの球状架橋ポ
リスチレン粒子0.1重量%と平均径0.45μmの球
状架橋ポリスチレン粒子0.025重量%配合)のペレ
ットを180℃で3時間真空乾燥した後に供給し、Tダ
イ中で合流し(積層比I/II=10/1)、表面温度3
0℃のキャストドラム上に静電気により密着させて冷却
固化し、積層未延伸キャストフィルムを得て、フィルム
厚みを5.5μmとした以外は、実施例4と同様の方法
で同時二軸延伸フィルムを得た。得られたフィルムのレ
ーザーラマン散乱法で得たピーク強度比R、ヤング率、
破れ頻度、ポリエチレンテレフタレートII面の耐摩耗
性、ポリエチレンテレフタレートI面に磁性層を塗布し
たフィルムの電磁変換特性を表5に示した。本発明のフ
ィルムは磁気記録媒体用として非常に適したものであっ
た。Example 5 Using two extruders A and B, polyethylene terephthalate I (having an intrinsic viscosity of 0.6) was heated to 280 ° C.
5. Glass transition temperature 75 ° C, melting point 255 ° C, average diameter 0.
Pellets of 2 μm spherical crosslinked polystyrene (blended with 0.2% by weight) were supplied after vacuum drying at 180 ° C. for 3 hours, and extruder B also heated to 280 ° C. was supplied with polyethylene terephthalate II (having an intrinsic viscosity of 0.65, A glass transition temperature of 75 ° C., a melting point of 255 ° C., and a pellet of 0.1% by weight of spherical crosslinked polystyrene particles having an average diameter of 0.3 μm and 0.025% by weight of spherical crosslinked polystyrene particles having an average diameter of 0.45 μm) were mixed at 180 ° C. Supply after vacuum drying for hours, merge in T-die (lamination ratio I / II = 10/1), surface temperature 3
A simultaneous biaxially stretched film was produced in the same manner as in Example 4, except that the film was cooled and solidified by being brought into close contact with static electricity on a cast drum at 0 ° C. to obtain a laminated unstretched cast film, and the film thickness was adjusted to 5.5 μm. Obtained. Peak intensity ratio R, Young's modulus, obtained by laser Raman scattering method of the obtained film,
Table 5 shows the breaking frequency, the abrasion resistance of the polyethylene terephthalate II surface, and the electromagnetic conversion characteristics of the film obtained by coating the magnetic layer on the polyethylene terephthalate I surface. The film of the present invention was very suitable for a magnetic recording medium.
【0060】[0060]
【表5】 [Table 5]
【0061】実施例6 ポリエチレンテレフタレート(固有粘度0.65、ガラ
ス転移温度75℃、融点255℃、平均径0.3μmの
凝集シリカ粒子0.2重量%配合)のペレットを180
℃で3時間真空乾燥した後に、280℃に加熱された押
出機に供給し、Tダイよりシート状に吐出した。さらに
このシートを表面温度25℃冷却ドラム上に静電気力で
密着させて冷却固化し、未延伸キャストフィルムを得
た。この未延伸フィルムの両端部をクリップで把持し
て、同時二軸延伸テンターに導き、110℃の温度で予
熱し、延伸倍率を縦方向に2倍、横方向に2倍とし、面
積延伸倍率4倍に第1段目の同時二軸延伸し、引続き8
0℃の温度で、延伸倍率を縦方向に3倍、横方向に3倍
とし、面積延伸倍率9倍に第2段目の同時二軸延伸した
後、さらに、160℃の温度で、延伸倍率を縦方向に
1.3倍、横方向に1.2倍とし、面積延伸倍率1.5
6倍に第3段目の同時二軸延伸した後、230℃の温度
で熱固定を施した後、150℃の冷却ゾーンで縦方向に
2%、横方向に3%の弛緩率で弛緩処理を行い、フィル
ムを室温に徐冷して巻取った。フィルム厚みは押出量を
調節して4.5μmに合わせた。この時のクリップ温度
は105℃とした。得られたフィルムのレーザーラマン
散乱法で得たピーク強度比R、ヤング率、長手方向の熱
収縮率(100℃×30分,%)、およびカラー印刷特
性を評価し表6に示した。表6に示したように熱転写リ
ボン用として非常に良好であった。Example 6 A pellet of polyethylene terephthalate (intrinsic viscosity: 0.65, glass transition temperature: 75 ° C., melting point: 255 ° C., 0.2% by weight of aggregated silica particles having an average diameter of 0.3 μm) was mixed with 180 pellets.
After vacuum drying at 3 ° C. for 3 hours, the mixture was supplied to an extruder heated to 280 ° C., and discharged from a T-die into a sheet. Further, this sheet was brought into close contact with a cooling drum having a surface temperature of 25 ° C. by electrostatic force and cooled and solidified to obtain an unstretched cast film. Both ends of the unstretched film are gripped with clips, guided to a simultaneous biaxial stretching tenter, preheated at a temperature of 110 ° C., stretched twice in the machine direction and twice in the transverse direction, and stretched in an area of 4 times. The first stage is simultaneously biaxially stretched twice,
At a temperature of 0 ° C., the stretching ratio is set to 3 times in the machine direction and 3 times in the transverse direction, and the second-stage simultaneous biaxial stretching is performed at an area stretching ratio of 9 times. Is 1.3 times in the longitudinal direction and 1.2 times in the lateral direction, and the area stretching ratio is 1.5.
After the simultaneous biaxial stretching of the third stage by 6 times, heat setting is performed at a temperature of 230 ° C, and then a relaxation treatment is performed at a cooling zone of 150 ° C with a relaxation rate of 2% in the vertical direction and 3% in the horizontal direction. The film was gradually cooled to room temperature and wound up. The film thickness was adjusted to 4.5 μm by adjusting the extrusion amount. The clip temperature at this time was 105 ° C. The peak intensity ratio R, Young's modulus, heat shrinkage in the longitudinal direction (100 ° C. × 30 minutes,%), and color printing characteristics of the obtained film, which were obtained by the laser Raman scattering method, were evaluated. As shown in Table 6, it was very good for a thermal transfer ribbon.
【0062】[0062]
【表6】 [Table 6]
【0063】実施例7 ポリエチレンテレフタレート(固有粘度0.65、ガラ
ス転移温度75℃、融点255℃、平均径0.2μmの
燐酸カルシウム粒子0.1重量%配合)のペレットを1
80℃で3時間真空乾燥した後に、280℃に加熱され
た押出機に供給し、Tダイよりシート状に吐出した。さ
らにこのシートを表面温度25℃冷却ドラム上に静電気
力で密着させて冷却固化し、未延伸キャストフィルムを
得た。この未延伸フィルムを、フィルム厚み3.5μ
m、熱固定温度220℃とした以外は、実施例6と同様
にして同時二軸延伸フィルムを得た。得られたフィルム
のレーザーラマン散乱法で得たピーク強度比R、ヤング
率、および幅方向、長手方向の破断伸度、コンデンサー
特性を表7に示した。表7から判るようにコンデンサー
用途として非常に良好であった。Example 7 A pellet of polyethylene terephthalate (having an intrinsic viscosity of 0.65, a glass transition temperature of 75 ° C., a melting point of 255 ° C., and containing 0.1% by weight of calcium phosphate particles having an average diameter of 0.2 μm) was mixed with 1 pellet.
After vacuum drying at 80 ° C. for 3 hours, the mixture was supplied to an extruder heated to 280 ° C., and discharged from a T-die into a sheet. Further, this sheet was brought into close contact with a cooling drum having a surface temperature of 25 ° C. by electrostatic force and cooled and solidified to obtain an unstretched cast film. This unstretched film is treated with a film
m, and a simultaneous biaxially stretched film was obtained in the same manner as in Example 6, except that the heat setting temperature was 220 ° C. Table 7 shows the peak intensity ratio R, Young's modulus, elongation at break in the width and length directions, and capacitor characteristics of the obtained film obtained by the laser Raman scattering method. As can be seen from Table 7, it was very good for use in capacitors.
【0064】[0064]
【表7】 [Table 7]
【0065】実施例8 ポリエチレンテレフタレート−ポリエチレンイソフタレ
ート共重合体(固有粘度0.70、ガラス転移点75
℃、融点225℃、共重合比80/20、平均径0.3
μmの凝集シリカ0.2重量%配合)のペレットを12
0℃で3時間真空乾燥して予備結晶化した後、180℃
で3時間真空乾燥し、しかる後に、270℃に加熱され
た押出機に供給し、Tダイよりシート状に吐出した。さ
らにこのシートを表面温度25℃の冷却ドラム上に静電
気力で密着させて冷却固化し、未延伸キャストフィルム
を得た。この未延伸フィルムの両端部をクリップで把持
して、同時二軸延伸テンターに導き、105℃の温度で
予熱し、延伸倍率を縦方向に2倍、横方向に2倍とし、
面積延伸倍率4倍に第1段目の同時二軸延伸し、引続き
75℃の温度で、延伸倍率を縦方向に3倍、横方向に3
倍とし、面積延伸倍率9倍に第2段目の同時二軸延伸し
た後、さらに、150℃の温度で、延伸倍率を縦方向に
1.3倍、横方向に1.3倍とし、面積延伸倍率1.6
9倍に第3段目の同時二軸延伸した後、120℃の温度
に冷却して、フィルムを室温に徐冷して巻取った。フィ
ルム厚みは押出量を調節して1.5μmとした。得られ
たフィルムの結晶融解熱ΔHuは25J/gであった。
レーザーラマン散乱法によるピーク強度比R、ヤング
率、表8に示した。このフィルムを目付量12g/m2
の和紙と貼り合わせ感熱孔版用原紙とした。この原紙を
用いてリソグラフ(理想化学工業社製)でテストパター
ン印刷をしたところ階調性も印字性能も優れたものであ
った。Example 8 Polyethylene terephthalate-polyethylene isophthalate copolymer (intrinsic viscosity 0.70, glass transition point 75
° C, melting point 225 ° C, copolymerization ratio 80/20, average diameter 0.3
pellets containing 0.2% by weight of agglomerated silica of 0.2 μm)
After pre-crystallization by vacuum drying at 0 ° C for 3 hours, 180 ° C
For 3 hours, and then supplied to an extruder heated to 270 ° C. and discharged from a T-die into a sheet. Further, this sheet was brought into close contact with a cooling drum having a surface temperature of 25 ° C. by electrostatic force and cooled and solidified to obtain an unstretched cast film. Both ends of this unstretched film are gripped with clips, guided to a simultaneous biaxial stretching tenter, and preheated at a temperature of 105 ° C., and the stretching ratio is twice in the machine direction and twice in the transverse direction.
The first stage is simultaneously biaxially stretched to an area stretching ratio of 4 times, and subsequently at a temperature of 75 ° C., the stretching ratio is 3 times in the longitudinal direction and 3 times in the horizontal direction.
After the simultaneous biaxial stretching of the second step at an area stretching ratio of 9 times, the stretching ratio was further increased at a temperature of 150 ° C. by 1.3 times in the longitudinal direction and 1.3 times in the horizontal direction. Stretch ratio 1.6
After the simultaneous biaxial stretching in the third stage at 9 times, the film was cooled to a temperature of 120 ° C., and the film was gradually cooled to room temperature and wound up. The film thickness was adjusted to 1.5 μm by adjusting the extrusion amount. The heat of crystal fusion ΔHu of the obtained film was 25 J / g.
The peak intensity ratio R and the Young's modulus according to the laser Raman scattering method are shown in Table 8. The weight of this film was 12 g / m 2.
Base paper for heat-sensitive stencil bonded with Japanese paper. When a test pattern was printed by lithography (manufactured by Riso Kagaku Kogyo Co., Ltd.) using this base paper, excellent gradation and printing performance were obtained.
【0066】[0066]
【表8】 [Table 8]
【0067】[0067]
【発明の効果】本発明の同時二軸延伸ポリエステルフィ
ルムおよびその製造方法によれば、フィルムの延伸破れ
を起さずに、高範囲の面積延伸倍率に延伸が可能とな
り、縦、横方向に高強度がされ、レーザーラマン散乱法
で測定した1615cm-1における縦方向と横方向の少
なくともいずれか一方の強度比Rを6以上とすること
で、高強度、耐摩耗性、寸法安定性、耐伸び性に優れた
フィルムを得ることができ、幅広い用途で使用すること
ができ、特に磁気記録媒体用途では、良好な特性を得る
ことができる。According to the simultaneous biaxially stretched polyester film of the present invention and the method for producing the same, it is possible to stretch the film in a wide range of the area stretching ratio without causing the film to be stretched and torn. By increasing the strength ratio R of at least one of the longitudinal direction and the transverse direction at 1615 cm -1 measured by the laser Raman scattering method to 6 or more, high strength, abrasion resistance, dimensional stability, and elongation resistance are obtained. A film having excellent properties can be obtained and can be used in a wide range of applications, and particularly in magnetic recording media, good characteristics can be obtained.
Claims (15)
テルのガラス転移温度Tg+25)℃〜(Tg+45)
℃の温度範囲で面積延伸倍率2〜7倍で縦および横方向
に同時二軸延伸する第1段目の延伸工程と、引続き(T
g−15)℃〜(Tg+10)℃の温度範囲で面積延伸
倍率4〜20倍で縦および横方向に同時二軸延伸する第
2段目の延伸工程を有することを特徴とする同時二軸延
伸ポリエステルフィルムの製造方法。1. An unstretched cast film is prepared by a method of (glass transition temperature of polyester Tg + 25) ° C. to (Tg + 45)
A first stretching step of simultaneously biaxially stretching in the longitudinal and transverse directions at an area stretching ratio of 2 to 7 times in a temperature range of ° C, followed by (T
g-15) Simultaneous biaxial stretching characterized by having a second stretching step of simultaneous biaxial stretching in the longitudinal and transverse directions at an area stretching ratio of 4 to 20 in the temperature range of (Tg + 10) ° C. Manufacturing method of polyester film.
各段階の延伸を行うことを特徴とする請求項1に記載の
同時二軸延伸ポリエステルフィルムの製造方法。2. The method for producing a simultaneously biaxially stretched polyester film according to claim 1, wherein the stretching in each step is performed when the difference between the longitudinal stretching ratio and the transverse stretching ratio is 1 or less.
テルのガラス転移温度Tg+25)℃〜(Tg+45)
℃の温度範囲で面積延伸倍率2〜7倍で縦および横方向
に同時二軸延伸する第1段目の延伸工程と、引続き(T
g−15)℃〜(Tg+10)℃の温度範囲で面積延伸
倍率4〜16倍で縦および横方向に同時二軸延伸する第
2段目の延伸工程と、さらに(ポリエステルの融解温度
Tm−130)℃〜(Tm−10)℃の温度範囲で面積
延伸倍率1.5〜5倍で縦および横方向に同時二軸延伸
する第3段目の延伸工程を有することを特徴とする同時
二軸延伸ポリエステルフィルムの製造方法。3. An unstretched cast film is prepared by heating (polyester glass transition temperature Tg + 25) ° C. to (Tg + 45)
A first stretching step of simultaneously biaxially stretching in the longitudinal and transverse directions at an area stretching ratio of 2 to 7 times in a temperature range of ° C, followed by (T
g-15) A second-stage stretching step of simultaneously biaxially stretching in the longitudinal and transverse directions at an area stretching ratio of 4 to 16 times in a temperature range of from 15 ° C. to (Tg + 10) ° C., and further (a melting temperature Tm-130 of the polyester). ) A simultaneous biaxial process comprising a third step of simultaneously performing biaxial stretching in the longitudinal and transverse directions at an area stretching ratio of 1.5 to 5 times in a temperature range of from ° C to (Tm-10) ° C. A method for producing a stretched polyester film.
で行うことを特徴とする請求項3に記載の同時二軸延伸
ポリエステルフィルムの製造方法。4. The method for producing a simultaneously biaxially stretched polyester film according to claim 3, wherein the third stage stretching is performed in a temperature range of two or more stages.
温度Tm−60)℃〜(Tm−10)℃の温度範囲で熱
固定を行い、熱固定温度からの冷却過程で縦および横方
向に弛緩処理を行うことを特徴とする請求項1〜4のい
ずれかに記載の同時二軸延伸ポリエステルフィルムの製
造方法。5. After the simultaneous biaxial stretching, heat fixing is performed in a temperature range of (melting temperature of polyester Tm-60) ° C. to (Tm-10) ° C .; The method for producing a simultaneous biaxially stretched polyester film according to any one of claims 1 to 4, wherein a relaxation treatment is performed.
ステルのガラス転移温度Tg+15)℃〜(Tg+5
0)℃の温度範囲にあることを特徴とする請求項1〜5
のいずれかに記載の同時二軸延伸ポリエステルフィルム
の製造方法。6. The temperature of the gripper at the film end is (glass transition temperature of polyester Tg + 15) ° C. to (Tg + 5).
0) It is in a temperature range of ° C.
The method for producing a simultaneous biaxially stretched polyester film according to any one of the above.
形状において、長手方向の長さ(LMD)と幅方向の長さ
(LTD)の比(LMD/LTD)が3〜15の範囲にあるこ
とを特徴とする請求項1〜6のいずれかに記載の同時二
軸延伸ポリエステルフィルムの製造方法。7. A surface of the film end and the gripper comes into contact shape, the ratio of the longitudinal length (L MD) and the width direction length (L TD) (L MD / L TD) is 3 The method for producing a simultaneously biaxially stretched polyester film according to any one of claims 1 to 6, wherein the polyester film is in a range of from 15 to 15.
走行具の駆動方式がリニアモータ方式であることを特徴
とする請求項1〜7のいずれかに記載の同時二軸延伸ポ
リエステルフィルムの製造方法。8. The simultaneous biaxially stretched polyester film according to any one of claims 1 to 7, wherein the driving system of the gripper of the tenter that performs simultaneous biaxial stretching is a linear motor system. Production method.
5cm-1における縦方向のピーク強度(IMD)と厚み方
向のピーク強度(IND)との比R1 (=IMD/IND)
と、横方向のピーク強度(ITD)と厚み方向のピーク強
度(IND)との比R2 (=ITD/IND)の少なくともい
ずれか一方が6以上であることを特徴とする同時二軸延
伸ポリエステルフィルム。9. 161 measured by a laser Raman scattering method
Ratio R 1 (= I MD / I ND ) between the peak intensity in the vertical direction ( IMD ) and the peak intensity in the thickness direction (I ND ) at 5 cm −1 .
And at least one of the ratio R 2 (= ITD / IND ) of the peak intensity in the lateral direction ( ITD ) to the peak intensity in the thickness direction ( IND ) is 6 or more. Biaxially stretched polyester film.
ヤング率(ETD)の少なくともいずれか一方が6GPa
以上であることを特徴とする請求項9に記載の同時二軸
延伸ポリエステルフィルム。10. At least one of the vertical Young's modulus (E MD ) and the horizontal Young's modulus (E TD ) is 6 GPa.
The simultaneous biaxially stretched polyester film according to claim 9, wherein:
レート、ポリプロピレンテレフタレート、ポリエチレン
イソフタレート、ポリエチレンナフタレートおよびこれ
らの共重合体より選ばれた少なくとも一種であることを
特徴とする請求項9または10に記載の同時二軸延伸ポ
リエステルフィルム。11. The simultaneous biaxial as claimed in claim 9, wherein the polyester is at least one selected from polyethylene terephthalate, polypropylene terephthalate, polyethylene isophthalate, polyethylene naphthalate and a copolymer thereof. Stretched polyester film.
以上であり、磁気記録媒体用であることを特徴とする請
求項9〜11のいずれかに記載の同時二軸延伸ポリエス
テルフィルム。12. lateral Young's modulus (E TD) is 6GPa
The simultaneous biaxially stretched polyester film according to any one of claims 9 to 11, which is for a magnetic recording medium.
縮率が2%以下であり、熱転写リボン用であることを特
徴とする請求項9〜11のいずれかに記載の同時二軸延
伸ポリエステルフィルム。13. The simultaneous biaxial stretching according to claim 9, wherein the thermal shrinkage in the longitudinal direction at 100 ° C. for 30 minutes is 2% or less, and is used for a thermal transfer ribbon. Polyester film.
0%以下であり、コンデンサー用であることを特徴とす
る請求項9〜11のいずれかに記載の同時二軸延伸ポリ
エステルフィルム。14. The film has an elongation at break of 10 in the longitudinal direction.
The simultaneous biaxially stretched polyester film according to any one of claims 9 to 11, wherein the polyester film content is 0% or less and used for a capacitor.
/g以下であり、感熱孔版印刷原紙用であることを特徴
とする請求項9〜11のいずれかに記載の二軸延伸ポリ
エステルフィルム。15. The film has a heat of crystal fusion ΔHu of 50 J.
/ G or less, and for heat-sensitive stencil printing base paper, the biaxially stretched polyester film according to any one of claims 9 to 11.
Priority Applications (12)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31898997A JP3726456B2 (en) | 1997-11-05 | 1997-11-05 | Simultaneously biaxially stretched polyester film and method for producing the same |
| CA 2249766 CA2249766A1 (en) | 1997-10-14 | 1998-10-07 | Biaxially oriented polyester films and their production methods |
| SG1998004096A SG76565A1 (en) | 1997-10-14 | 1998-10-07 | Biaxially oriented polyester films and their production methods |
| TW87116697A TW411316B (en) | 1997-10-14 | 1998-10-08 | Biaxially oriented polyester films and their production methods |
| EP19980119107 EP0909780B1 (en) | 1997-10-14 | 1998-10-09 | Biaxially oriented polyester films and their production methods |
| DE1998637904 DE69837904T2 (en) | 1997-10-14 | 1998-10-09 | Biaxially oriented polyester films and their production process |
| MYPI98004674A MY117927A (en) | 1997-10-14 | 1998-10-13 | Biaxially oriented polyester films and their production methods |
| US09/172,119 US6197430B1 (en) | 1997-10-14 | 1998-10-14 | Biaxially oriented polyester films and their production methods |
| CN98124521A CN1107584C (en) | 1997-10-14 | 1998-10-14 | Double shaft oriented polyester and its preparing method |
| KR1019980043007A KR100554045B1 (en) | 1997-10-14 | 1998-10-14 | Biaxially Oriented Polyester Films and their Production Methods |
| ID981362A ID21071A (en) | 1997-10-14 | 1998-10-14 | MULTIPLE SHORT POLYESTER FILM AND ITS PRODUCT METHOD |
| US09/697,489 US6562274B1 (en) | 1997-10-14 | 2000-10-27 | Process of making biaxially oriented polyester films |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31898997A JP3726456B2 (en) | 1997-11-05 | 1997-11-05 | Simultaneously biaxially stretched polyester film and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH11138629A true JPH11138629A (en) | 1999-05-25 |
| JP3726456B2 JP3726456B2 (en) | 2005-12-14 |
Family
ID=18105258
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31898997A Expired - Lifetime JP3726456B2 (en) | 1997-10-14 | 1997-11-05 | Simultaneously biaxially stretched polyester film and method for producing the same |
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| Country | Link |
|---|---|
| JP (1) | JP3726456B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20000067585A (en) * | 1999-04-29 | 2000-11-25 | 장용균 | the Process of Biaxial-oriented Polyester film Manufacture |
| JP2001049005A (en) * | 1999-08-11 | 2001-02-20 | Toray Ind Inc | Biaxially oriented polyester film and its preparation |
| WO2017131373A1 (en) * | 2016-01-29 | 2017-08-03 | (주)효성 | Method for manufacturing polyester film by using simultaneous biaxial stretching method |
| CN114619659A (en) * | 2022-05-16 | 2022-06-14 | 河南银金达新材料股份有限公司 | Low-density lightweight polyester film stretching process |
-
1997
- 1997-11-05 JP JP31898997A patent/JP3726456B2/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20000067585A (en) * | 1999-04-29 | 2000-11-25 | 장용균 | the Process of Biaxial-oriented Polyester film Manufacture |
| JP2001049005A (en) * | 1999-08-11 | 2001-02-20 | Toray Ind Inc | Biaxially oriented polyester film and its preparation |
| WO2017131373A1 (en) * | 2016-01-29 | 2017-08-03 | (주)효성 | Method for manufacturing polyester film by using simultaneous biaxial stretching method |
| CN114619659A (en) * | 2022-05-16 | 2022-06-14 | 河南银金达新材料股份有限公司 | Low-density lightweight polyester film stretching process |
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|---|---|
| JP3726456B2 (en) | 2005-12-14 |
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