JPS6360731A - Preparation of biaxially oriented polyethylene-2,6-naphthalate film having high strength in longitudinal direction - Google Patents
Preparation of biaxially oriented polyethylene-2,6-naphthalate film having high strength in longitudinal directionInfo
- Publication number
- JPS6360731A JPS6360731A JP20545386A JP20545386A JPS6360731A JP S6360731 A JPS6360731 A JP S6360731A JP 20545386 A JP20545386 A JP 20545386A JP 20545386 A JP20545386 A JP 20545386A JP S6360731 A JPS6360731 A JP S6360731A
- Authority
- JP
- Japan
- Prior art keywords
- film
- longitudinal direction
- stretching
- temperature
- less
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 238000009998 heat setting Methods 0.000 claims abstract description 7
- 230000007704 transition Effects 0.000 claims abstract description 5
- 230000002040 relaxant effect Effects 0.000 claims description 3
- 239000000853 adhesive Substances 0.000 claims description 2
- 230000001070 adhesive effect Effects 0.000 claims description 2
- 239000010408 film Substances 0.000 description 78
- -1 polyethylene Polymers 0.000 description 30
- 238000000034 method Methods 0.000 description 21
- 239000004698 Polyethylene Substances 0.000 description 12
- 229920000573 polyethylene Polymers 0.000 description 12
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 8
- 229920000139 polyethylene terephthalate Polymers 0.000 description 8
- 239000005020 polyethylene terephthalate Substances 0.000 description 8
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 5
- UOBYKYZJUGYBDK-UHFFFAOYSA-N 2-naphthoic acid Chemical compound C1=CC=CC2=CC(C(=O)O)=CC=C21 UOBYKYZJUGYBDK-UHFFFAOYSA-N 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229920003207 poly(ethylene-2,6-naphthalate) Polymers 0.000 description 4
- 239000011112 polyethylene naphthalate Substances 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 150000002736 metal compounds Chemical class 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- QPUYECUOLPXSFR-UHFFFAOYSA-N 1-methylnaphthalene Chemical compound C1=CC=C2C(C)=CC=CC2=C1 QPUYECUOLPXSFR-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 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
- 239000006229 carbon black Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000000806 elastomer Substances 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical compound [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- 239000005995 Aluminium silicate Substances 0.000 description 1
- 101100247319 Drosophila melanogaster Ras64B gene Proteins 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- ALQSHHUCVQOPAS-UHFFFAOYSA-N Pentane-1,5-diol Chemical compound OCCCCCO ALQSHHUCVQOPAS-UHFFFAOYSA-N 0.000 description 1
- 235000014676 Phragmites communis Nutrition 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- AYJRCSIUFZENHW-DEQYMQKBSA-L barium(2+);oxomethanediolate Chemical compound [Ba+2].[O-][14C]([O-])=O AYJRCSIUFZENHW-DEQYMQKBSA-L 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- QXDMQSPYEZFLGF-UHFFFAOYSA-L calcium oxalate Chemical compound [Ca+2].[O-]C(=O)C([O-])=O QXDMQSPYEZFLGF-UHFFFAOYSA-L 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 239000012770 industrial material Substances 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
- 229910001386 lithium phosphate Inorganic materials 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- GVALZJMUIHGIMD-UHFFFAOYSA-H magnesium phosphate Chemical compound [Mg+2].[Mg+2].[Mg+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O GVALZJMUIHGIMD-UHFFFAOYSA-H 0.000 description 1
- 239000004137 magnesium phosphate Substances 0.000 description 1
- 229910000157 magnesium phosphate Inorganic materials 0.000 description 1
- 229960002261 magnesium phosphate Drugs 0.000 description 1
- 235000010994 magnesium phosphates Nutrition 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- ISIJQEHRDSCQIU-UHFFFAOYSA-N tert-butyl 2,7-diazaspiro[4.5]decane-7-carboxylate Chemical compound C1N(C(=O)OC(C)(C)C)CCCC11CNCC1 ISIJQEHRDSCQIU-UHFFFAOYSA-N 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 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 1
- TWQULNDIKKJZPH-UHFFFAOYSA-K trilithium;phosphate Chemical compound [Li+].[Li+].[Li+].[O-]P([O-])([O-])=O TWQULNDIKKJZPH-UHFFFAOYSA-K 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、長手方向の強度の極めて役れ/ζポリエチレ
ンーー、6−ナフタL’−ドア(ルムノg造法に関する
。更に詳しくは、縦横の厚さ斑の極めて少ない縦高強カ
ニ軸配向ポリエチレンーコ、6−す7タレートフイルム
の製造法に関する。Detailed Description of the Invention [Industrial Application Field] The present invention relates to a door with extremely high strength in the longitudinal direction / The present invention relates to a method for producing a 6-7 tallate film made of strong crab-axis oriented polyethylene film with very little thickness unevenness.
〔従来の技術と発明が解決しようとする問題点〕周知の
ごとく、近年工業材料用フィルムとしては、ポリエチレ
ンテレフタレートフィルムが主流である。このポリエチ
レンテレフタレートは、種々の使用分野において薄膜化
が望まれ、縦方向強力化フィルムが使用されているが、
工業的規模で製造するにはせいぜいヤング率が100〜
900 Kg/1m’程度であシ、現在要望されている
/100Kv−以上のヤング率には到達し得ない。一方
これに対しポリエチレンーコ、6−す7タレートでは、
ylooKyy値2以上の高強度フィルムが知られてい
る(%開昭!fO−100/クダ号公報、特開昭30−
10コ30J号公報参照)。[Prior art and problems to be solved by the invention] As is well known, in recent years polyethylene terephthalate films have become mainstream as films for industrial materials. This polyethylene terephthalate is desired to be made into a thin film in various fields of use, and a longitudinally reinforced film is used.
For production on an industrial scale, the Young's modulus must be at most 100~
The Young's modulus is about 900 Kg/1 m' and cannot reach the currently desired Young's modulus of /100 Kv- or more. On the other hand, polyethylene co, 6-s7 talate,
High-strength films with a ylooKyy value of 2 or more are known (% Kaisho!
(Refer to Publication No. 10/30J).
ポリエチレン−2,6−ナフタレートはポリエチレンテ
レフタレートに比べて、結晶化速度が極めて遅く、延伸
による配向結晶化を極力抑制した状態で、ポリエチレン
テレフタレートに比べて格段に高い面積倍率を達成する
事ができ、縦方向高強力フィルムを製造するには、極め
て適した材料であることが知られている。Polyethylene-2,6-naphthalate has an extremely slow crystallization rate compared to polyethylene terephthalate, and can achieve a much higher area magnification than polyethylene terephthalate while suppressing oriented crystallization due to stretching as much as possible. It is known to be an extremely suitable material for producing high strength longitudinal films.
しかしながら、結晶化速度が遅いという性質は、高強度
フィルムを製造する点に関しては、有利であるが、厚み
が揃いにくいという欠点を有する。この為、縦方向のヤ
ング率が/10θに9/!j以上であって、縦横共に厚
さ斑の極めて小さなフィルムを製造する際には、単に延
伸倍率を高めるだけでは不可能であり、極めて厳密に管
理された製造プロセスを採用する事によってのみ可能と
々るものである。However, although the property of having a slow crystallization rate is advantageous in producing a high-strength film, it has the disadvantage that it is difficult to make the thickness uniform. Therefore, the Young's modulus in the longitudinal direction becomes /10θ9/! When producing a film with extremely small thickness unevenness in both length and width, it is impossible to simply increase the stretching ratio, and it is possible only by adopting an extremely strictly controlled manufacturing process. There are many things.
本発明は、前記のごとき要求を満たすべく検討されたも
のであり、その目的は、縦方向のヤング率が/ / 0
0 K4/wa”以上であってかつ縦横の厚さ斑の極め
て少ないフィルムの製造方法を提供することにある。The present invention has been studied to satisfy the above-mentioned requirements, and its purpose is to have a Young's modulus in the longitudinal direction of / / 0
It is an object of the present invention to provide a method for producing a film which has a film thickness of 0 K4/wa" or more and has very little variation in thickness in the vertical and horizontal directions.
本発明者らは、上記目的を達成すべく鋭意検討の結果、
ポリエチレンーコ、6−ナフタレートの延伸に際し、あ
る特定の延伸製膜条件を採用することにより、上記目的
を達成し得ることを見出し、本発明に到達したものであ
る。As a result of intensive studies to achieve the above object, the inventors of the present invention found that
The present invention was achieved by discovering that the above object can be achieved by employing certain stretching film forming conditions when stretching polyethylene co-6-naphthalate.
すなわち本発明の要旨は、実質的に無配向のポリエチレ
ンーコ、6−す7タレートの未延伸フィルムを、まず縦
方向に二次転移点より10℃高い温度以上ロールとの粘
着温度以下の温度で且つ、配向率が10%以上40%以
下となるように延伸したのち、更に縦方向に前記延伸温
度以上ロール粘着温度以下の温度で且つ、配向率がUO
%以上60%以下となるように延伸し、次いで横方向の
屈折率が縦方向の屈折率よりも高くなるように横方向に
3,5倍以上横延伸して二軸配向フィルムとなし、更に
該二軸配向フィルムを横延伸温度以上230℃以下の温
度で熱固定すると共に、巾方向に3チ乃至30%巾弛緩
したのち、上記熱固定温度以下で再縦延伸し、しかる後
、必要に応じて熱固定し、縦方向のヤング率が/ /
00 Ky/wn2以上、縦方向の屈折率が7300以
上、厚さ方向の屈折率が/JOO以下で且つ縦、損失々
の厚さ斑がf%以下のフィルムとなすことを特像とする
縦方向高張カニ軸配向ポリエチレンーー、6−す7タレ
ートフイルムの製造法に存する。That is, the gist of the present invention is to first heat an unstretched film of substantially unoriented polyethylene co-6-7 tallate in the longitudinal direction at a temperature higher than the secondary transition point by 10°C and lower than the adhesion temperature with a roll. And after stretching so that the orientation ratio is 10% or more and 40% or less, the film is further stretched in the longitudinal direction at a temperature higher than the stretching temperature and lower than the roll adhesion temperature, and the orientation ratio is UO.
% or more and 60% or less, and then transversely stretched 3.5 times or more in the transverse direction so that the refractive index in the transverse direction is higher than the refractive index in the longitudinal direction to form a biaxially oriented film, and further The biaxially oriented film is heat set at a temperature higher than or equal to the transverse stretching temperature and lower than 230°C, and relaxed by 3 to 30% in the width direction, and then longitudinally stretched again at the above heat setting temperature, and then stretched as necessary. Heat set according to the longitudinal Young's modulus / /
00 Ky/wn2 or more, a longitudinal refractive index of 7300 or more, a thickness direction refractive index of /JOO or less, and a thickness unevenness in the longitudinal direction and loss of f% or less. Directional hypertonic crab-axis oriented polyethylene - a method for producing a 6-7 tallate film.
本発明でいうポリエチレン一一、6−ナフタレートとは
、その構成単位が実質的にエチレン−,2,A−す7タ
レ一ト単位から構成されているポリマーを指すが、少量
例えば、10モルチ以下好ましくは5モルチ以下の第3
成分によって変性されたエチレンm=、6−す7タレー
トボリマーも含まれる。Polyethylene 11,6-naphthalate as used in the present invention refers to a polymer whose constituent units are substantially composed of ethylene-,2,A-7-thale units, but in small amounts, for example, 10 mole or less. Preferably less than 5 molt.
Also included are ethylene m=6-7 tallate polymers modified by components.
ポリエチレン一一、6−ナフタレートは、一般にナフタ
レンーコ、6−ジカルボン酸又はその機能的誘導体例え
ばナフタレンーコ、6−ジカルボン酸メチル等と、エチ
レングリコールとを触媒の存在下で適尚な反応条件の下
に縮合させることによって製造される。その場合ナフタ
レンーコ、6−ジカルボン醗及びエチレングリコール以
外の第3成分として例えばアジピン敢、シュウ酸、イン
7タル酸、テレフタル酸、ナフタレンーコ、7−ジカル
ボン酸、ジフェニルエーテルジカルボン酸等のジカルボ
ン酸又はその低級アルキルエステル;p−オキシ安息香
酸、p−オキシエトキシ安息香酸のごときオキシカルボ
ン酸又はその低級アルキルエステル;或いは、グロビレ
ングリコール、トリメチレングリコール。Polyethylene 11,6-naphthalate is generally produced by condensing naphthalene, 6-dicarboxylic acid, or a functional derivative thereof, such as methyl naphthalene or 6-dicarboxylate, with ethylene glycol in the presence of a catalyst under appropriate reaction conditions. Manufactured by In that case, as a third component other than naphthalene, 6-dicarboxylic acid and ethylene glycol, dicarboxylic acids such as adipine acid, oxalic acid, di-7thalic acid, terephthalic acid, naphthalene, 7-dicarboxylic acid, diphenyl ether dicarboxylic acid, or lower alkyl thereof. Esters; oxycarboxylic acids such as p-oxybenzoic acid and p-oxyethoxybenzoic acid or lower alkyl esters thereof; or globylene glycol, trimethylene glycol.
テトラメチレングリコール、ペンタメチレングリコール
、ヘキサメチレングリコール、ジエチレングリコール、
/、t−シクロヘキサンジメタノール等のコ価アルコー
ル;ポリエチレングリコール、ポリテトラメチレングリ
コールのごときポリアルキレングリコール等を挙げるこ
とができる0又、重合に際して、二酸化チタン等の艶消
剤、カーボンブラック等の遮光剤、リン酸。Tetramethylene glycol, pentamethylene glycol, hexamethylene glycol, diethylene glycol,
/, covalent alcohols such as t-cyclohexanedimethanol; polyalkylene glycols such as polyethylene glycol and polytetramethylene glycol; and during polymerization, matting agents such as titanium dioxide, light shielding agents such as carbon black, etc. agent, phosphoric acid.
亜リン酸及びこれらのエステル等の安定剤、ヒンダード
フェノール等の酸化防止剤9重合調節剤、結晶化調節剤
、可塑剤等を添加しても差しつかえない。Stabilizers such as phosphorous acid and their esters, antioxidants such as hindered phenols, polymerization regulators, crystallization regulators, plasticizers, etc. may be added.
又、本発明で用いるポリエチレンナフタレートは、重合
度が低すぎると、機械的特性が低下するので、その極限
粘度は、O,lIO以上好ましくは0.6〜O,デのも
のである。Furthermore, if the degree of polymerization of the polyethylene naphthalate used in the present invention is too low, the mechanical properties will deteriorate, so the intrinsic viscosity thereof is 0.1IO or more, preferably 0.6 to 0.0.
本発明のフィルムは、各種用途例えば磁気テープ用途、
感熱転写用途、コンデンサー用途等種々の用途に使用す
ることができるが、いずれの用途に用いる場合も、走行
性を与えるために、微細な不活性化合物を含有せしめて
滑り性を付与させる必要がある。かかる方法のひとつに
は、ポリエチレンナフタレート製造時に、反応系内に溶
存している金属化合物例えばエステル交換反応後系内に
溶存している金属化合物にリン化合物を作用させて、微
細な粒子を析出させる方法、いわゆる析出粒子法がある
。該手法は、特に粗大粒子が少なく、好ましい手法であ
るが、簡便な手法として今ひとつの手法いわゆる添加粒
子法がより好ましく用いられる。The film of the present invention can be used for various purposes such as magnetic tape use,
It can be used for a variety of purposes such as thermal transfer and capacitor applications, but for any purpose, it is necessary to contain a fine inert compound to impart slipperiness in order to provide runnability. . One such method is to precipitate fine particles by causing a phosphorus compound to act on a metal compound dissolved in the reaction system during the production of polyethylene naphthalate, such as a metal compound dissolved in the system after transesterification. There is a method called the precipitated particle method. This method is particularly preferable since it produces fewer coarse particles, but as a simpler method, another method, the so-called additive particle method, is more preferably used.
ここで添加粒子法とは、ポリエチレンナフタレート製造
工程から、製膜前の押出工程のいずれかの工程でポリエ
チレンナフタレート重合体原料中に、不活性な微細粒子
を配合せしめる方法であシ、この不活性微粒子としては
、例えばカオリン、タルク、炭酸マグネシウム、炭酸カ
ルシウム、炭酸バリウム、硫酸カルシウム、リン酸リチ
ウム、リン酸カルシウム、リン酸マグネシウム、WI化
アルミニウム、酸化ケイ素、酸化チタン、フッ化リチウ
ム、シュウ酸カルシウム及び(!a、Ba、Zn、Mn
等のテレフタル酸塩等から選ばれ九/種以上の金属化合
物あるいはカーボンブラック等を挙げることができる。Here, the additive particle method is a method in which inert fine particles are blended into the polyethylene naphthalate polymer raw material at any step from the polyethylene naphthalate production process to the extrusion process before film formation. Examples of inert fine particles include kaolin, talc, magnesium carbonate, calcium carbonate, barium carbonate, calcium sulfate, lithium phosphate, calcium phosphate, magnesium phosphate, aluminum oxide, silicon oxide, titanium oxide, lithium fluoride, and calcium oxalate. and (!a, Ba, Zn, Mn
Examples include nine or more metal compounds selected from terephthalates such as, carbon black, and the like.
この不活性化合物の形状は、球状、塊状、あるいは偏平
状のいずれであっても良くまたその硬度。The shape of this inert compound may be spherical, lumpy, or flat, and its hardness may vary.
比重9色等についても特に制限はない。該不活性化合物
の平均粒径は、通常等価球直径で0./〜70μ好まし
くは0,3〜3μの範囲から選ばれる。又そのフィルム
に対する配合量は、o、oi〜10重量%好ましくは、
0.02〜o3重量−更に好ましくは、0.OJ〜O1
S重量%の範囲から選択される。There is no particular restriction on the nine specific gravity colors, etc. The average particle size of the inert compound is usually an equivalent spherical diameter of 0. /~70μ, preferably from 0.3~3μ. The amount of the film to be blended is preferably o, oi to 10% by weight,
0.02 to o3 weight - more preferably 0.02 to o3 weight. OJ~O1
S is selected from a range of % by weight.
本発明においては、公知の手段で乾燥し溶融押出後冷却
ドラム上にキャストした実質的に無配向のポリエチレン
ーコ、6−ナフタレートの未延伸フィルムをまず縦方向
に延伸する。ポリエチレンーコ、6−ナフタレートの縦
延伸に際し重要な側面のひとつは、延伸ロールの材質で
ある。In the present invention, a substantially non-oriented unstretched film of polyethylene, 6-naphthalate, which is dried by a known method, melt-extruded, and then cast on a cooling drum, is first stretched in the longitudinal direction. One of the important aspects in the longitudinal stretching of polyethylene co-6-naphthalate is the material of the stretching rolls.
通常ポリエチレンテレフタレートの延伸に際しては、フ
ィルムのスリ傷防止、平滑性の維持を目的としてハード
クロムメッキによる鏡面ロールが用いられている。しか
しながら後述するごトくポリエチレン−2,A−ナフタ
レートの延伸では、ハードクロムメッキした鏡面ロール
では、フィルムの厚さ斑を良好にできる延伸温度では、
フィルムとの粘着が生じてしまうため不適である。一方
フイルムとの粘着を防止するロールとシテ、テフロン系
、シリコン系等のエラストマーライニングロールが知ら
れているが、工業的規模での生産に使用するに際しては
、耐久性特に耐摩耗性が弱く使用困難である。それ故ポ
リエテレンーコ、6−す7タレートの縦延伸ロールとし
ては、ハードクロムメッキロールよりも非粘着性に優れ
、耐久性も良好なセラミックコートロールを使用するこ
とが好ましい。セラミックコートロールの材質としては
、At、O,等公知の材質を使用できる。又、表面粗度
も用途によって異なるが0./BからよSの間で用いる
ことが好ましい。Normally, when polyethylene terephthalate is stretched, mirror-finished rolls plated with hard chrome are used to prevent scratches on the film and maintain smoothness. However, in the stretching of polyethylene-2,A-naphthalate, which will be described later, with a hard chrome-plated mirror roll, at a stretching temperature that can improve the unevenness of the film thickness,
This is unsuitable because it causes adhesion to the film. On the other hand, rolls and rolls lined with elastomers such as shite, Teflon, and silicone are known to prevent adhesion to the film, but when used in industrial scale production, they have poor durability, especially wear resistance. Have difficulty. Therefore, it is preferable to use a ceramic-coated roll, which has better non-adhesiveness and better durability than a hard chrome-plated roll, as a longitudinal stretching roll for polyester resin and 6-7 tallate. As the material of the ceramic coat roll, known materials such as At, O, etc. can be used. Also, the surface roughness varies depending on the application, but it is 0. It is preferable to use between /B and yoS.
かくしてセラミックコートロールを縦延伸ロールとして
用いて縦延伸する際、本発明においては、多段延伸する
ことが必須である。−段で延伸する事も可能であるが、
−段階による延伸によυ縦方向の厚さ斑を市販のポリエ
チレンテレフタl/−)フィルム並(R/x−約3チ)
とするためには、延伸温度を極めて高温にする必要があ
るが、ロールとの粘着が生じてしまうため、商品価値が
無くなってしまい不適である。本発明において、縦延伸
を多段階で行なう際まず、前述の未延伸フィルムを、二
次転移点(約//3℃)より70℃高い温度以上、ロー
ルとの粘着温度(/E+のセラミックコートロールで約
7≠θ℃)以下の温度で7段階又は多段階延伸し、配向
率が10%以上l60%以下となるようにまず延伸する
ことが必要である。この延伸過程を以後”前段延伸″と
称する。ここでボリエテレンーコ、6−ナフタレートの
最大軸配向複屈折率Hrm (Δn)は、共重合度の度
合い等により異なるがほぼθ、3左である。延伸温度が
二次転移点以下では、冷延伸となシフイルムに厚薄が生
じ以後の延伸によっても厚さ斑が改良されず不適である
。一方延伸温度は高ければ高い程良いがロールと粘着す
る温度を超えると、フィルムに表面欠陥が生じ不適であ
る。又、該前段延伸において、配向率が10%より小さ
い場合、フィルムの配向が低い為以後の延伸温度を高く
することが困難となるので、厚さ斑改良が困難となう不
適である。一方前段延伸での配向率がtI0チを超えて
しまうと、後段の延伸倍率を高く取ることができずこの
場合も厚さ斑改良が困難と々シ、不適である。好ましく
は、JO%以下更に好ましくは、2!チ以下である。Thus, when performing longitudinal stretching using a ceramic coated roll as a longitudinal stretching roll, multistage stretching is essential in the present invention. - Although it is possible to stretch in stages,
- The thickness unevenness in the vertical direction is reduced by stepwise stretching to the same level as commercially available polyethylene terephthalate film (R/x - about 3 inches)
In order to achieve this, it is necessary to set the stretching temperature to an extremely high temperature, but this is unsuitable because it causes adhesion to the rolls and thus loses its commercial value. In the present invention, when longitudinal stretching is carried out in multiple stages, the unstretched film is heated at a temperature higher than 70°C higher than the secondary transition point (approx. It is necessary to first stretch the film in 7 stages or in multiple stages using a roll at a temperature of about 7≠θ°C or lower so that the orientation ratio is 10% or more and 160% or less. This stretching process will be referred to as "pre-stage stretching" hereinafter. Here, the maximum axial orientation birefringence Hrm (Δn) of borie terenco and 6-naphthalate is approximately θ, 3, although it varies depending on the degree of copolymerization and the like. If the stretching temperature is below the secondary transition point, the film will become thick and thin during cold stretching, and the thickness unevenness will not be improved by subsequent stretching, which is unsuitable. On the other hand, the higher the stretching temperature, the better; however, if it exceeds the temperature at which the film sticks to the roll, surface defects will occur in the film, which is unsuitable. Furthermore, if the orientation ratio in the first stage stretching is less than 10%, it is difficult to increase the subsequent stretching temperature because the orientation of the film is low, making it difficult to improve thickness unevenness, which is unsuitable. On the other hand, if the orientation ratio in the first stage stretching exceeds tI0, it is impossible to obtain a high stretching ratio in the second stage, and in this case as well, it is difficult to improve thickness unevenness and is therefore unsuitable. Preferably JO% or less, more preferably 2! less than or equal to
かくして得られた前段メ延伸フィルムは、更に縦方向に
前段延伸温度以上、ロール粘着温度以下の温度で延伸し
、配向率がダO%以上60チ以下となるよう延伸し縦延
伸フィルムを得る。The pre-stretched film thus obtained is further stretched in the longitudinal direction at a temperature above the pre-stretching temperature and below the roll adhesion temperature to obtain a longitudinally stretched film with an orientation ratio of 0% to 60 cm.
該延伸工程を以後゛後段延伸″と称す。後段延伸は配向
率がダθチ以上60チ以下の範囲で行なう限り多段でも
良いが/段階で行うのが好ましい。後段延伸温度は、前
段延伸温度以上であることが必要である0前段延伸温度
より低いと厚さ斑が改良されない。一方後段延伸のロー
ルとの粘着温度は、前段延伸に比べて極めて高くなって
いる。前段延伸に対する後段延伸での粘着温度の上昇は
、前段延伸の配向率に依存し、前段延伸後の配向率が高
い程高く々るため・前段延伸の配向率は、出来るだけ高
くすることが好ましい。後段延伸後の配向率は、yo%
以上60%以下である。後段延伸後の配向率がダθ係よ
り低い場合は、縦方向の厚さ斑の改良が見られず不適で
ある。一方60%を超えると、以後の横延伸、再延伸工
程で破断が頻発し製膜困難となり不適である。This stretching process is hereinafter referred to as "second-stage stretching".The second-stage stretching may be carried out in multiple stages as long as the orientation ratio is within the range of 60 cm or more, but it is preferably performed in stages.The second-stage stretching temperature is the same as the first-stage stretching temperature. If the temperature is lower than the first-stage stretching temperature, the thickness unevenness will not be improved.On the other hand, the adhesion temperature with the rolls in the second-stage stretching is extremely high compared to the first-stage stretching. The increase in adhesion temperature depends on the orientation ratio of the first-stage stretching, and increases as the orientation ratio after the first-stage stretching increases.It is preferable to make the orientation ratio of the first-stage stretching as high as possible.Orientation after the second-stage stretching The rate is yo%
60% or less. If the orientation ratio after the post-stretching is lower than the Da θ coefficient, no improvement in thickness unevenness in the longitudinal direction is observed, which is unsuitable. On the other hand, if it exceeds 60%, breakage occurs frequently in the subsequent transverse stretching and re-stretching steps, making it difficult to form a film, making it unsuitable.
上述したごとく、前段延伸後そのまま後段延伸に移行し
ても良いが、本発明においては、後段延伸前に配向緩和
のための熱緩和工程を含めることも厚さ斑改良のために
好ましい手法である。配向緩和は、ロールで行なっても
良いし、赤外線ヒーター等外部加熱方式で行なってもよ
い。配向緩和の為の熱処理は、処理直前の縦延伸温度以
上ロールとの粘着温度以下で0.5〜3.0秒、/、0
7倍からへ/倍の延伸倍率に押さえて行なう事が好まし
い。熱緩和をロールで行なう際のロールとしては、ハー
ドクロムメッキロール、セラミックコートロール以外で
も、テフロンロール、シリコンロール等エラストマーロ
ールを使用することも延伸をほとんど行なわないため可
能である。As mentioned above, after the first-stage stretching, it is possible to proceed directly to the second-stage stretching, but in the present invention, it is also a preferable method for improving thickness unevenness to include a thermal relaxation step for orientation relaxation before the second-stage stretching. . Orientation relaxation may be performed using a roll, or may be performed using an external heating method such as an infrared heater. Heat treatment for orientation relaxation is carried out at a temperature higher than the longitudinal stretching temperature immediately before treatment and lower than the adhesion temperature with the roll for 0.5 to 3.0 seconds, /,0
It is preferable to keep the stretching ratio from 7 times to 7 times. In addition to hard chrome plated rolls and ceramic coated rolls, it is also possible to use elastomer rolls such as Teflon rolls and silicone rolls as rolls for thermal relaxation, since stretching is hardly performed.
かくして得られた縦−軸延伸フィルムは、−般にテンタ
ーよりなる横方向延伸工程に送られ、/20℃〜/りO
℃好ましくは/3θ℃〜/60℃で3.3倍以上横方向
に延伸される。その際横方向の屈折率が縦方向の屈折率
より高くなる様延伸する事が必須である。この工程での
フィルムが縦に配向している場合には、再延伸の後横方
向の厚さ斑を揃えるのが極めて困難となり不適である。The longitudinally-axially stretched film thus obtained is sent to a transverse stretching step, which generally consists of a tenter, at temperatures ranging from /20°C to /20°C.
The film is stretched in the transverse direction at a temperature of 3.3 times or more at a temperature of preferably /3θ°C to /60°C. At that time, it is essential to stretch so that the refractive index in the transverse direction is higher than the refractive index in the longitudinal direction. If the film in this step is oriented vertically, it will be extremely difficult to even out the thickness unevenness in the lateral direction after re-stretching, which is unsuitable.
次に、該二軸配向フィルムは横延伸温度以上230℃以
下の温度で熱固定に供される。この工程での熱固定は、
次の再延伸工程において、フィルムが巾方向に収縮する
ことによる破断を防止するためと共に再延伸工程での強
度増加を助長するために必須の工程である。更に、この
工程もしくは該工程の後火の再延伸工程前に、フィルム
を巾方向に、7%乃至30%巾弛緩することが必須であ
る。この巾弛緩工程なしで次の再延伸を行なう場合、巾
方向の配向が大きすぎるため縦方向の強度を所定の値に
する前に破断が頻発し不適である。それ故山弛緩として
は3%以上好ましくは3%以上が必要である。−方巾弛
緩が30%を超えると、横方向のフィルムの厚さ斑が極
度に悪化してしまうので好ましくない。好ましくは−よ
%以下更に好ましくは20%以下である。Next, the biaxially oriented film is subjected to heat setting at a temperature above the transverse stretching temperature and below 230°C. The heat fixation in this process is
This is an essential step in order to prevent the film from breaking due to shrinkage in the width direction in the next re-stretching step, and to promote an increase in strength in the re-stretching step. Furthermore, it is essential to relax the film in the width direction by 7% to 30% before this step or the post-fire re-stretching step of the step. If the next re-stretching is performed without this width relaxing step, the orientation in the width direction is too large, which is unsuitable because breakage occurs frequently before the strength in the machine direction reaches a predetermined value. Therefore, the mountain relaxation needs to be 3% or more, preferably 3% or more. - If the width relaxation exceeds 30%, it is not preferable because the thickness unevenness of the film in the lateral direction becomes extremely worse. It is preferably -1% or less, more preferably 20% or less.
かくして得られたフィルムを更に縦方向に再延伸する。The film thus obtained is further stretched again in the machine direction.
該再延伸に際しては、縦−段延伸が最も好ましいが、必
要に応じて、縦二段延伸、再縦−再横−再縦延伸、再横
−再縦延伸又、縦。For the re-stretching, longitudinal-stage stretching is most preferable, but if necessary, longitudinal two-stage stretching, longitudinal-re-transverse-re-longitudinal stretching, re-transverse-re-longitudinal stretching, or longitudinal stretching.
横同時延伸等行なうことは、問題ない。There is no problem with simultaneous transverse stretching.
しかるのち、用途に応じて熱固定して製品化されるが、
このフィルムの縦方向のヤング率は/ / 00 Kt
v’m”以上、縦方向の屈折率は/、100以上、厚さ
方向の屈折率は/、! 00以下且つ、縦横の厚さ斑が
ざチ以下でちる事が必須である。Afterwards, it is heat-set and manufactured into a product depending on the purpose.
The Young's modulus of this film in the longitudinal direction is / / 00 Kt
It is essential that the refractive index in the vertical direction is /,100 or more, the refractive index in the thickness direction is /,!00 or less, and the vertical and horizontal thickness unevenness is less than or equal to 100.
縦方向のヤング率が/ / 00 Kg/ras2より
低い場合はポリエチレンテレフタレートでも達成可能で
アシ、ポリエチレンーコ、6−ナフタレートを使用する
利点がなく好ましくない。より好ましくは/ J 00
K4/m”以上更に好ましくは/ 300 K9/r
m”以上である。又、縦方向の屈折率が/、ざ00より
低い場合もしくは厚さ方向の屈折率が/、!;00を超
えるフィルムにおいても、縦方向のヤング率が//θθ
陵−以上のフィルムを得ることができるが、この場合に
は、横力向の強度が弱く不適である。If the Young's modulus in the longitudinal direction is lower than / / 00 Kg/ras2, it can be achieved with polyethylene terephthalate, and there is no advantage of using reed, polyethylene, or 6-naphthalate, which is not preferred. More preferably / J 00
K4/m" or more, more preferably / 300 K9/r
If the refractive index in the longitudinal direction is lower than /, 00, or the refractive index in the thickness direction exceeds /, !;00, the Young's modulus in the longitudinal direction is
Although it is possible to obtain a film with a thickness of 100 mm or more, the strength in the direction of lateral force is low and it is unsuitable in this case.
以上述べたごとく、本発明方法によれば、ポリエチレン
ーコ、6−ナフタレートの縦横共に厚さ斑が少なくしか
も縦方向の強度に極めて優れたフィルムを得る事が可能
となり、これまでポリエチレンテレフタレートフィルム
では使用不可能であった種々の高品質高性能フィルム用
途に適用可能となるので、本発明方法は極めて工業的価
値に優れるものである。As described above, according to the method of the present invention, it is possible to obtain a film of polyethylene co-6-naphthalate that has less unevenness in thickness both vertically and horizontally and has extremely excellent strength in the vertical direction. The method of the present invention has extremely excellent industrial value because it can be applied to various high-quality, high-performance film applications that have previously been impossible.
以下、実施例により本発明を具体的に説明するが、本発
明はその要旨を越えない限シ以下の実施例に限定される
ものではない。なお、フィルムの諸物性の測定方法は、
次の通シである。Hereinafter, the present invention will be explained in detail with reference to examples, but the present invention is not limited to the following examples as long as the gist thereof is not exceeded. The method for measuring the physical properties of the film is as follows:
This is the following circular.
(1)厚さ斑
安立電気社製連続フィルム厚さ測定器(電子マイクロメ
ーター使用)によりニ軸延伸フィルムの縦及び横方向に
沿って測定し、3m長さについて次式によυ算出した。(1) Thickness The thickness was measured along the longitudinal and lateral directions of the biaxially stretched film using a continuous film thickness measuring device (using an electronic micrometer) manufactured by Madarasu Ritsu Electric Co., Ltd., and υ was calculated for a length of 3 m using the following formula.
カールツアイス社製偏光顕微鏡にて縦延伸フィルムのり
タープ−ジョンを測定し、次式により複屈折率Δnを求
めた。The longitudinally stretched film adhesive tarpsion was measured using a polarizing microscope manufactured by Carl Zeiss, and the birefringence Δn was determined using the following formula.
1m−R/d R:リターデーションd:フイルム
厚さ
く3)屈折率
アタゴ社製アツベ式屈折計にてコ3℃で長手方向及び厚
さ方向の屈折率を常法により測定した。1 m-R/d R: Retardation d: Film thickness 3) Refractive index The refractive index in the longitudinal direction and the thickness direction was measured at 3° C. using an Atsube refractometer manufactured by Atago Co., Ltd. by a conventional method.
(4)フィルム温度
バーンズ社製赤外線放射温度計により延伸部のフィルム
温度を測定した。(4) Film temperature The temperature of the film at the stretched portion was measured using an infrared radiation thermometer manufactured by Burns.
(5)粘着によるフィルム表面欠陥
アルミニウム蒸着フィルム表面をカールツアイス社製微
分干渉顕微鏡で観察。フィルム表面に対し凸部を形成す
るタテスジ状傷がj本/−以上あるものを欠陥のあるフ
ィルムとして×、S本/−未満のものをフィルム欠陥の
ないフィルムとして○で表示した。(5) Film surface defects due to adhesion The surface of the aluminum evaporated film was observed using a Carl Zeiss differential interference microscope. A film with J/- or more vertical scratches forming convex portions on the film surface was marked as a defective film, and a film with less than S scratches/- was marked as a film with no film defects.
比較例/、λ実施例/、λ
ポリエチレンーコ、6−ナフタレート((n) =0.
63)を常法により乾燥後、溶融押出をし、静電密着法
により、冷却ドラム上にキャストして実質的に無配向の
未延伸フィルムを採取した。Comparative Example/, λ Example/, λ Polyethyleneco, 6-naphthalate ((n) = 0.
63) was dried by a conventional method, melt-extruded, and cast onto a cooling drum by an electrostatic adhesion method to obtain a substantially non-oriented unstretched film.
該未延伸フィルムをまず縦方向に延伸したがその際粗度
/8のセラミックコートした延伸ロールを用いたが、ロ
ールとの粘着温度はユ、0倍延伸した際/’40℃であ
ったので、粘着温度以下の131℃で/、−倍(比較例
/ )、/、1倍(実施例1)、ユ、!I倍(実施例、
2 ) 、 、7..2倍(比較例2)前段延伸を行な
い、更に横延伸並総合倍率がJ、1倍となるようiso
℃で延伸したのち/&、MCで9.0倍横延伸し760
℃で巾方向に70%弛緩しながら熱固定して、753℃
でへ53倍再縦延伸後コθO℃で熱固定して7μのフィ
ルムを得た。このフィルムの評価結果を表7に示す。The unstretched film was first stretched in the longitudinal direction using a ceramic-coated stretching roll with a roughness of 8, but the adhesion temperature with the roll was 40°C when stretched 0 times. , at 131°C below the adhesion temperature /, - times (comparative example / ), /, 1 times (Example 1), Yu,! I times (Example,
2), ,7. .. 2 times (Comparative Example 2) Perform the first-stage stretching, and further stretch the ISO so that the total magnification is J, 1 times
After stretching at °C, /&, 9.0 times horizontal stretching at MC to 760
Heat set at 753°C while relaxing 70% in the width direction.
After longitudinal stretching again by 53 times, the film was heat-set at θ0° C. to obtain a 7 μm film. Table 7 shows the evaluation results of this film.
比較例3
実施例−において、横延伸並総合倍率を7.3倍とした
ところ横延伸時破断が多発してフィルム化できなかった
。Comparative Example 3 In Example--, when the overall magnification for horizontal stretching was set to 7.3 times, the film could not be formed into a film due to frequent breaks during horizontal stretching.
比較例弘
実施例−において横延伸倍率を3.0倍とする以外は、
実施例二と同様に製膜し7μのフィルムを得た。Comparative Example Hiroshi Example - except that the lateral stretch ratio was 3.0 times,
A film of 7μ was obtained by forming a film in the same manner as in Example 2.
比較例よ
実施例コにおいて、巾方向の弛緩を0%とする以外実施
例コと同様に延伸しようとしたが再縦延伸倍率をへ3倍
以上にすると破断が多発した0
比較例6
実施例−において弛緩率を3−%として7μのフィルム
を得た。Comparative Example In Example C, stretching was attempted in the same manner as in Example C except that the relaxation in the width direction was set to 0%, but when the re-longitudinal stretching ratio was increased to 3 times or more, breakage occurred frequently.Comparative Example 6 Example A film of 7μ was obtained with a relaxation rate of 3% at -.
比較例7、実施例3、ダ
実施例コにおいて横延伸後の熱固定を行なわないで延伸
したところ、再縦延伸時フィルムの耳部がふれ破断が多
発した。一方、実施例λにおいて横延伸後の熱固定温度
を710℃、200℃として製膜した。In Comparative Example 7, Example 3, and Example 3, when stretching was performed without heat setting after transverse stretching, the edges of the film ran out and broke frequently during longitudinal stretching. On the other hand, in Example λ, films were formed at heat setting temperatures of 710° C. and 200° C. after transverse stretching.
これらの結果を表7に示す。These results are shown in Table 7.
表7の結果から明らかな如く、本逼発明の方法によれば
、ポリエチレン一一、6−ナフタレートフィルムにおい
ても、ポリエチレンテレフタレート並の厚さ斑の均一な
フィルムでかつ縦方向の強度の高いフィルムを得ること
ができ、工業用フィルムとして、極めて好適なフィルム
を得ることが可能となる。As is clear from the results in Table 7, according to the method of the present invention, even in polyethylene 11,6-naphthalate films, films with uniform thickness unevenness comparable to polyethylene terephthalate and high strength in the longitudinal direction can be obtained. This makes it possible to obtain a film that is extremely suitable as an industrial film.
出 願 人 ダイアホイル株式会社 代 理 人 弁理士長香川 − ほか/名Sender: Diafoil Co., Ltd. Representative Patent Attorney Naga Kagawa - Others/names
Claims (1)
レートの未延伸フィルムを、まず縦方向に二次転移点よ
り10℃高い温度以上ロールとの粘着温度以下の温度で
且つ配向率が10%以上40%以下となるように延伸し
たのち、更に縦方向に前記延伸温度以上、ロール粘着温
度以下の温度で且つ配向率が40%以上 60%以下となるように延伸し、次いで、横方向の屈折
率が縦方向の屈折率よりも高くなるように横方向に3.
5倍以上横延伸して二軸配向フィルムとなし、更に、該
二軸配向フィルムを横延伸温度以上230℃以下の温度
で熱固定すると共に巾方向に3%乃至30%巾弛緩した
のち、上記熱固定温度以下で再縦延伸し、しかる後、必
要に応じて熱固定し、縦方向のヤング率が1,100K
g/mm^2以上、縦方向の屈折率が1,800以上、
厚さ方向の屈折率が1,500以下で且つ縦、横夫々の
厚さ斑が8%以下のフィルムとなすことを特徴とする縦
方向高強力二軸配向ポリエチレン−2,6−ナフタレー
トフィルムの製造法。(1) A substantially unoriented unstretched film of polyethylene-2,6-naphthalate is first heated in the longitudinal direction at a temperature that is 10°C higher than the secondary transition point and lower than the adhesive temperature with the roll, and at an orientation rate of 10°C. % or more and 40% or less, and then further stretched in the longitudinal direction at a temperature not less than the stretching temperature and not more than the roll adhesion temperature and with an orientation rate of 40% or more and 60% or less, and then in the transverse direction. 3. in the horizontal direction so that the refractive index is higher than the refractive index in the vertical direction.
After transversely stretching 5 times or more to obtain a biaxially oriented film, and further heat-setting the biaxially oriented film at a temperature above the transverse stretching temperature and below 230°C and relaxing it by 3% to 30% in the width direction, the above-mentioned Re-stretch longitudinally at a temperature below the heat-setting temperature, then heat-set if necessary, until the Young's modulus in the longitudinal direction is 1,100K.
g/mm^2 or more, longitudinal refractive index 1,800 or more,
A biaxially oriented polyethylene-2,6-naphthalate film with high strength in the longitudinal direction, which has a refractive index in the thickness direction of 1,500 or less and a thickness unevenness in both the longitudinal and lateral directions of 8% or less. manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20545386A JPS6360731A (en) | 1986-09-01 | 1986-09-01 | Preparation of biaxially oriented polyethylene-2,6-naphthalate film having high strength in longitudinal direction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20545386A JPS6360731A (en) | 1986-09-01 | 1986-09-01 | Preparation of biaxially oriented polyethylene-2,6-naphthalate film having high strength in longitudinal direction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6360731A true JPS6360731A (en) | 1988-03-16 |
Family
ID=16507129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20545386A Pending JPS6360731A (en) | 1986-09-01 | 1986-09-01 | Preparation of biaxially oriented polyethylene-2,6-naphthalate film having high strength in longitudinal direction |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6360731A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0659809A2 (en) | 1993-12-22 | 1995-06-28 | Teijin Limited | Biaxially oriented film of polyethylene-2,6-naphthalenedicarboxylate |
| JP2002240143A (en) * | 2001-02-22 | 2002-08-28 | Toray Ind Inc | Method for producing polyester film |
-
1986
- 1986-09-01 JP JP20545386A patent/JPS6360731A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0659809A2 (en) | 1993-12-22 | 1995-06-28 | Teijin Limited | Biaxially oriented film of polyethylene-2,6-naphthalenedicarboxylate |
| US5631063A (en) * | 1993-12-22 | 1997-05-20 | Teijin Limited | Biaxially oriented film of polyethylene-2,6-naphthalenedicarboxylate |
| JP2002240143A (en) * | 2001-02-22 | 2002-08-28 | Toray Ind Inc | Method for producing polyester film |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5662317B2 (en) | Polyester film and method for producing the same | |
| KR0158461B1 (en) | Biaxially Oriented Polyethylene-2,6-naphthalenedicarboxylate Film and Manufacturing Method Thereof | |
| JP3569077B2 (en) | Polyester film for large-sized molded transfer foil | |
| JPH0379178B2 (en) | ||
| JPH03137814A (en) | Biaxially oriented polyester film for floppy disk | |
| EP0390191B1 (en) | Biaxially stretched polyester film and process for producing the same | |
| US4610833A (en) | Process for preparing biaxially stretched polyester films | |
| KR20190078121A (en) | Polyester film for molding and manufacturing method thereof | |
| JP3804311B2 (en) | Polyester film and method for producing the same | |
| JPH09300892A (en) | Polyester film for transfer foil | |
| JPH0832499B2 (en) | Heat resistant polyester film for transfer film | |
| JPH0832498B2 (en) | Polyester film for transfer film | |
| KR0157090B1 (en) | Biaxial oriented polyester film | |
| TW396106B (en) | Biaxially oriented film of polyethylene -2, 6-Naphthalenedicarboxylate | |
| JP2943183B2 (en) | Laminated molding | |
| JPH02130125A (en) | Production of polyester film | |
| JPS6360732A (en) | Polyethylene-2,6-naphthalate film | |
| JPH0425855B2 (en) | ||
| JP2611413B2 (en) | Method for producing high-strength polyester film | |
| JPH0415729B2 (en) | ||
| JP2003221497A (en) | Polyester film for embossing | |
| JPH0324936A (en) | Biaxial oriented polyester film | |
| KR0157089B1 (en) | Biaxial oriented polyester film | |
| JP2555707B2 (en) | Process for producing polyethylene 2,6-naphthalate film | |
| JPH0371976B2 (en) |