TWI632053B - Biaxially oriented polyester film - Google Patents

Biaxially oriented polyester film Download PDF

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TWI632053B
TWI632053B TW103122201A TW103122201A TWI632053B TW I632053 B TWI632053 B TW I632053B TW 103122201 A TW103122201 A TW 103122201A TW 103122201 A TW103122201 A TW 103122201A TW I632053 B TWI632053 B TW I632053B
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film
width
temperature
biaxially oriented
oriented polyester
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TW103122201A
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TW201509640A (en
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真鍋功
莊司秀夫
高田育
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東麗股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/91Heating, e.g. for cross linking
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/914Cooling of flat articles, e.g. using specially adapted supporting means cooling drums
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
    • B29C48/9165Electrostatic pinning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/80Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/86Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the nozzle zone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/918Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling
    • B29C48/9185Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling in the direction of the stream of the material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02Polyesters derived from dicarboxylic acids and dihydroxy compounds

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Materials Engineering (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Laminated Bodies (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Polarising Elements (AREA)

Abstract

本發明之課題在於提供一種成型性、寬度方向物性均勻性優異,可適合用於成型加工用、光學用之雙軸配向聚酯薄膜。 An object of the present invention is to provide a biaxially-oriented polyester film which is excellent in moldability and uniformity in physical properties in the width direction and can be suitably used for molding processing and optical applications.

本發明之解決手段為一種雙軸配向聚酯薄膜,其在150℃的薄膜MD(machine direction,縱向)方向之10%伸張時應力為5MPa以上30MPa以下,在150℃的薄膜MD方向之熱收縮率為5%以下,且1000mm寬度中的薄膜之配向角(主配向軸與薄膜TD(transverse direction,橫向)方向或薄膜MD方向所成之角度中小者的角度)之最大值為20°以下。 The solution of the present invention is a biaxially oriented polyester film, which has a stress of 5 MPa or more and 30 MPa or less when stretched at 10% of the MD (machine direction) direction of the film at 150 ° C, and thermal shrinkage of the film in the MD direction at 150 ° C. The ratio is 5% or less, and the maximum value of the alignment angle (the angle of the smaller of the angle formed by the main alignment axis and the TD (transverse direction) direction or the MD direction of the film) of the film is 20 ° or less.

惟,1000mm寬度的薄膜之配向角,係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心,沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜,於自該任意之點起往TD方向兩端在50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm之位置(1000mm寬度),測定配向角,求得其中之最大值;而且,於同一薄膜面內將與TD方向呈正交的方向設為MD方向。 However, the alignment angle of a film with a width of 1000 mm is to set the main alignment axis direction of any position of the film to the TD direction. With this position as the center, take a width of 550 mm in two directions along the TD direction to make a film with a width of 1100 mm , From the arbitrary point to the two ends in the TD direction at 50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 450mm, and 500mm (1000mm width), measure the alignment angle, and find the maximum value ; In the same film plane, the direction orthogonal to the TD direction is set to the MD direction.

Description

雙軸配向聚酯薄膜 Biaxially oriented polyester film

本發明關於雙軸配向聚酯薄膜,關於特別適用於成型加工用途、光學用途之雙軸配向聚酯薄膜。 The present invention relates to a biaxially oriented polyester film, and relates to a biaxially oriented polyester film that is particularly suitable for molding processing and optical applications.

近年來,由於環境意識的升高,於建材、汽車零件或行動電話、電機製品等中,強烈需求無溶劑塗裝、鍍敷替代等,使用薄膜的裝飾方法之導入係正在進展。 In recent years, due to the rise in environmental awareness, there is a strong demand for solvent-free coating, plating replacement, etc. in building materials, automotive parts, mobile phones, and electrical products. The introduction of decorative methods using thin films is progressing.

作為該裝飾方法中所使用的成型用聚酯薄膜,有幾個提案。例如,有提案即使於低溫下也顯示低成型應力、低儲存彈性模數,滿足高易成型性之成型用聚酯薄膜(例如參照專利文獻1)。 As a polyester film for molding used in this decoration method, several proposals have been made. For example, there is a proposal for a polyester film for molding that exhibits low molding stress, low modulus of storage elasticity, and satisfies high moldability even at low temperatures (for example, refer to Patent Document 1).

又,亦有提案於低溫下顯示高儲存彈性模數,於高溫下顯示低成型應力,使耐熱性與成型性並存之聚酯薄膜(例如參照專利文獻2)。 There is also a proposal for a polyester film that exhibits a high storage elastic modulus at a low temperature, a low molding stress at a high temperature, and a combination of heat resistance and moldability (for example, refer to Patent Document 2).

另外,液晶顯示器係使用於大型電視、個人電腦、平板、智慧型手機等,今後亦預計穩定的需求。構成液晶顯示器的偏光板,係使用表面保護薄膜、脫模薄膜、相位差薄膜、工程薄膜等各式各樣的薄膜,寬度方向的物性之均勻性係非常重要,作為雙軸延伸聚酯薄膜,亦有幾個提案。例如,有提案為了滿足寬度方向的均勻性 ,使配向角與厚度不均減低之偏光薄膜貼合用聚酯薄膜(例如參照專利文獻3)。又,隨著智慧型手機、平板終端等之智慧型裝置的擴大,液晶顯示器薄膜化之要求提高,於偏光板‧相位差層中亦往高精細化、薄膜化進展。因此,為了達成相位差層的高精細化、薄膜化,在工程薄膜上塗布相位差層,連工程薄膜一起成型,而達成相位差層的高精細化、薄膜化之製程開發係正在進展。 In addition, liquid crystal displays are used in large TVs, personal computers, tablets, and smartphones, and stable demand is expected in the future. The polarizing plate constituting the liquid crystal display uses various films such as a surface protection film, a release film, a retardation film, and an engineering film. The uniformity of the physical properties in the width direction is very important. As a biaxially stretched polyester film, There are also several proposals. For example, there are proposals to satisfy the uniformity in the width direction A polyester film for polarizing film bonding that reduces unevenness in alignment angle and thickness (for example, refer to Patent Document 3). In addition, with the expansion of smart devices such as smart phones and tablet terminals, the demand for thin filming of liquid crystal displays has increased, and high-definition and thin-filming has also progressed in polarizing plates and retardation layers. Therefore, in order to achieve high-definition and thin-film formation of the retardation layer, a process retardation layer is coated on the engineering film and molded together with the engineering film, and the process development system for achieving high-definition and thin-film formation of the retardation layer is progressing.

[先前技術文獻] [Prior technical literature] [專利文獻] [Patent Literature]

[專利文獻1]日本特開2005-290354號公報 [Patent Document 1] Japanese Patent Laid-Open No. 2005-290354

[專利文獻2]國際公開第2012-005097號 [Patent Document 2] International Publication No. 2012-005097

[專利文獻3]日本特開2002-40249號公報 [Patent Document 3] Japanese Patent Laid-Open No. 2002-40249

然而,專利文獻1、2中記載的薄膜,雖然成型性優異,但由於寬度方向的物性不均勻,使用於大型構件的裝飾成型等時,會發生成型不均或成型後的應變不均。又,若作為偏光板‧相位差層的工程薄膜使用,則由於物性不均勻,故會發生特性不均。 However, although the films described in Patent Documents 1 and 2 are excellent in moldability, they are uneven in physical properties in the width direction, and when they are used for decorative molding of large members, uneven molding or uneven strain after molding may occur. Moreover, if it is used as an engineering film of a polarizing plate and a retardation layer, uneven physical properties may cause uneven characteristics.

又,專利文獻3中記載之薄膜,雖然寬度方向的均勻性優異,但由於成型性不充分,對於深形狀的裝飾成型或連工程薄膜一起成型的偏光板‧相位差,係難以使用。 Moreover, although the film described in Patent Document 3 is excellent in uniformity in the width direction, it is difficult to use it because it has insufficient moldability for deep-shaped decorative molding or polarizing plates and phase differences formed with an engineering film.

本發明之課題在於消除上述習知技術的問題 點。即,提供一種雙軸配向聚酯薄膜,其係成型性、寬度方向物性均勻性優異,可適用於成型加工用、光學用者。 The object of the present invention is to eliminate the problems of the conventional techniques described above. point. That is, a biaxially-oriented polyester film is provided, which is excellent in moldability and uniformity in physical properties in the width direction, and is suitable for use in molding and optical applications.

為了解決該問題,本發明之要旨係如以下。 To solve this problem, the gist of the present invention is as follows.

一種雙軸配向聚酯薄膜,其在150℃的薄膜MD(Machine direction,縱向,以下稱為MD)方向之10%伸張時應力為5MPa以上30MPa以下,在150℃的薄膜MD方向之熱收縮率為5%以下,且1000mm寬度的薄膜之配向角{(主配向軸與薄膜TD(Transverse Direction,橫向,以下稱為TD)方向或薄膜MD方向所成之角度中小者的角度)}之最大值為20。以下。惟,1000mm寬度的薄膜之配向角,係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心,沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜,於自該任意之點起往TD方向兩端在50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm之位置(1000mm寬度),測定配向角,求得其中之最大值;而且,於同一薄膜面內將與TD方向呈正交的方向設為MD方向。 A biaxially oriented polyester film having a thermal contraction rate of 150 MPa or more and a stress of 5 MPa or less at 10% of the MD (Machine direction, hereinafter referred to as MD) direction of the film at 150 ° C, and the MD direction of the film at 150 ° C The maximum value of the alignment angle of a film with a width of less than 5% and a thickness of 1000 mm {(the angle of the smaller of the angle formed by the main alignment axis and the film in the TD (Transverse Direction, transverse direction) or MD direction of the film)} Is 20. the following. However, the alignment angle of a film with a width of 1000 mm is to set the main alignment axis direction of any position of the film to the TD direction. With this position as the center, take a width of 550 mm in two directions along the TD direction to make a film with a width of 1100 mm. , From the arbitrary point to the two ends in the TD direction at 50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 450mm, and 500mm (1000mm width), measure the alignment angle, and find the maximum value ; In the same film plane, the direction orthogonal to the TD direction is set to the MD direction.

本發明之雙軸配向聚酯薄膜,由於在150℃的成型應力低,易成型性良好,而且由於150℃之熱收縮率低,塗布乾燥時的薄膜變形小,更且由於1000mm寬度的薄膜之配向角的最大值小,寬度方向之物性均勻性優異,可適用於建材、行動機器、電機製品、汽車零件、遊 戲機零件等之成型裝飾用途、偏光板等之光學用薄膜等。 The biaxially oriented polyester film of the present invention has low forming stress at 150 ° C and good moldability, and because of the low thermal shrinkage at 150 ° C, the film deformation during coating and drying is small, and because of the 1000mm width film, The maximum value of the alignment angle is small, and the physical property uniformity in the width direction is excellent. It can be applied to building materials, mobile machines, electrical products, automotive parts, and tourism. It is used for molding and decoration of theater parts, and for optical films such as polarizing plates.

[實施發明之形態] [Form of Implementing Invention]

所謂構成本發明之雙軸配向聚酯薄膜的聚酯,就是主鏈中的主要鍵結為酯鍵之高分子化合物的總稱。而且,聚酯樹脂通常係可藉由使二羧酸或其衍生物與二醇或其衍生物進行聚縮合反應而得。 The polyester constituting the biaxially oriented polyester film of the present invention is a general term for a polymer compound whose main bond in the main chain is an ester bond. The polyester resin is usually obtained by subjecting a dicarboxylic acid or a derivative thereof to a polycondensation reaction with a diol or a derivative thereof.

於本發明中,從成型性、外觀、耐熱性、尺寸安定性、經濟性之方面來看,構成聚酯的二醇單元之60莫耳%以上較佳為來自乙二醇的結構單元,二羧酸單元之60莫耳%以上較佳為來自對苯二甲酸的結構單元。再者於此,所謂二羧酸單元(結構單元)或二醇單元(結構單元),就是意指已去掉經由聚縮合去除的部分後之2價有機基,若需要,由以下之通式表示。 In the present invention, from the aspects of moldability, appearance, heat resistance, dimensional stability, and economy, more than 60 mol% of the diol units constituting the polyester are preferably structural units derived from ethylene glycol. 60 mol% or more of the carboxylic acid unit is preferably a structural unit derived from terephthalic acid. Here, the so-called dicarboxylic acid unit (structural unit) or diol unit (structural unit) means a divalent organic group in which a portion removed by polycondensation has been removed, and if necessary, it is represented by the following general formula .

二羧酸單元(結構單元):-CO-R-CO- Dicarboxylic acid unit (structural unit): -CO-R-CO-

二醇單元(結構單元):-O-R’-O- Diol unit (structural unit): -O-R'-O-

(此處,R、R’係二價有機基) (Here, R and R 'are divalent organic groups)

再者,於包含偏苯三酸單元或甘油單元等3價以上之羧酸或醇以及彼等之衍生物時,關於3價以上的羧酸或醇單元(結構單元),亦同樣地意指已去掉經由聚縮合去除的部分後之3價以上的有機基。 In addition, when a trivalent or higher carboxylic acid or alcohol and a derivative thereof including a trimellitic acid unit or a glycerol unit are included, the same applies to a trivalent or higher carboxylic acid or alcohol unit (structural unit). The trivalent or more organic group after removing the part removed by polycondensation has been removed.

作為給予本發明中使用的聚酯之二醇或其衍生物,除了乙二醇,還可舉出二乙二醇、1,2-丙二醇、 1,3-丙二醇、1,3-丁二醇、1,4-丁二醇、1,5-戊二醇、1,6-己二醇、新戊二醇等之脂肪族二羥基化合物、二乙二醇、聚乙二醇、聚丙二醇、聚四亞甲基二醇等之聚氧化烯(polyoxyalkylene)二醇、1,4-環己烷二甲醇、螺二醇等之脂環族二羥基化合物、雙酚A、雙酚S等之芳香族二羥基化合物、以及彼等之衍生物。其中,於成型性、操作性之方面,較宜使用二乙二醇、1,3-丙二醇、1,4-丁二醇、新戊二醇、1,4-環己烷二甲醇。 Examples of the diol or its derivative to be used for the polyester used in the present invention include diethylene glycol, 1,2-propylene glycol, and Aliphatic dihydroxy compounds such as 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, neopentyl glycol, etc. Polyoxyalkylene glycols such as diethylene glycol, polyethylene glycol, polypropylene glycol, polytetramethylene glycol, etc., cycloaliphatic diene such as 1,4-cyclohexanedimethanol, spirodiol, etc. Aromatic dihydroxy compounds such as hydroxy compounds, bisphenol A, bisphenol S, and their derivatives. Among these, diethylene glycol, 1,3-propanediol, 1,4-butanediol, neopentyl glycol, and 1,4-cyclohexanedimethanol are more preferably used in terms of moldability and operability.

又,作為給予本發明中使用的聚酯之二羧酸 或其衍生物,除了對苯二甲酸,還可舉出間苯二甲酸、苯二甲酸、2,6-萘二羧酸、二苯基二羧酸、二苯基磺二羧酸、二苯氧基乙烷二羧酸、5-鈉磺二羧酸等之芳香族二羧酸、草酸、琥珀酸、己二酸、癸二酸、二聚酸、馬來酸、富馬酸等之脂肪族二羧酸、1,4-環己烷二羧酸等之脂環族二羧酸、對羥基苯甲酸等之羥基羧酸、以及彼等之衍生物。作為二羧酸之衍生物,可舉出例如對苯二甲酸二甲酯、對苯二甲酸二乙酯、對苯二甲酸2-羥基乙基甲酯、2,6-萘二羧酸二甲酯、間苯二甲酸二甲酯、己二酸二甲酯、馬來酸二乙酯、二聚酸二甲酯等之酯化物。其中,於成型性、操作性之方面,較宜使用間苯二甲酸、2,6-萘二羧酸、1,4-環己烷二羧酸及彼等之酯化物。 Also, as a dicarboxylic acid to be used for the polyester used in the present invention Or its derivative, in addition to terephthalic acid, isophthalic acid, phthalic acid, 2,6-naphthalenedicarboxylic acid, diphenyldicarboxylic acid, diphenylsulfodicarboxylic acid, dibenzene Fatty acids such as oxyethanedicarboxylic acid, 5-sodium disulfonic acid, etc., oxalic acid, succinic acid, adipic acid, sebacic acid, dimer acid, maleic acid, fumaric acid, etc. Alicyclic dicarboxylic acids such as dicarboxylic acids, 1,4-cyclohexanedicarboxylic acids, hydroxycarboxylic acids such as parahydroxybenzoic acid, and their derivatives. Examples of the dicarboxylic acid derivatives include dimethyl terephthalate, diethyl terephthalate, 2-hydroxyethyl methyl terephthalate, and dimethyl 2,6-naphthalene dicarboxylate. Esters, esters of dimethyl isophthalate, dimethyl adipate, diethyl maleate, dimethyl dimer, etc. Among them, in terms of moldability and operability, isophthalic acid, 2,6-naphthalenedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, and their esterified products are more preferably used.

本發明之雙軸配向聚酯薄膜,為了滿足對複 雜形狀的賦形性、連工程薄膜一起成型時的易成型性,故在150℃的薄膜MD方向10%伸張時應力必須為5MPa以上30MPa以下。 The biaxially oriented polyester film of the present invention Due to the heterogeneous shape forming ability and the ease of forming when the engineering film is molded together, the stress must be 5 MPa to 30 MPa when the film is stretched at 10% in the MD direction at 150 ° C.

此處,於本發明中,1000mm寬度薄膜之評價,係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,對於自1100mm寬度之薄膜的TD方向中心起沿著TD方向的2方向中之500mm寬度(1000mm寬度),進行評價。本發明之聚酯薄膜較佳為MD方向10m以上、TD方向1100mm以上之大小。 Here, in the present invention, the evaluation of a film having a width of 1000 mm is to set the main alignment axis direction of an arbitrary position of the film to the TD direction, and use that position as the center (hereinafter also referred to as the TD direction center), and follow the TD direction to A width of 550 mm was taken in each of the two directions, and a 500 mm width (1000 mm width) of the two directions along the TD direction from the center of the TD direction of the 1100 mm film was evaluated. The polyester film of the present invention preferably has a size of 10 m or more in the MD direction and 1100 mm or more in the TD direction.

又,所謂在150℃的薄膜MD方向10%伸張時應力,就是表示將經切出成試驗長度50mm的矩形型之薄膜樣品,在經預先設定在150℃的恆溫槽中,固定薄膜樣品,於90秒的預熱後,以300mm/分鐘之應變速度進行拉伸試驗之際,樣品伸張10%伸張時之施加於薄膜的應力。再者,評價係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,在1100mm寬度之薄膜的TD方向中心、自TD方向中心起TD方向的任意之一方向(A方向)的500mm之位置、自TD方向中心起TD方向之與A方向相反的方向(B方向)之500mm之位置的3點,各自進行5次,將其15個之值的平均值設為在150℃的薄膜MD方向10%伸張時應力。從成型性、尺寸安定性之觀點來看,在150℃的薄膜MD方向10%伸張時應力,若為6MPa以上20MPa以下則更佳,若為7MPa以上15MPa以下則最佳。 In addition, the so-called stress at 10% stretching in the MD direction of a film at 150 ° C means that a rectangular film sample cut into a test length of 50 mm is fixed in a thermostatic bath set at 150 ° C in advance, and After a preheating time of 90 seconds, when the tensile test was performed at a strain rate of 300 mm / min, the stress applied to the film when the sample was stretched by 10%. In addition, the evaluation is to set the main alignment axis direction of the arbitrary position of the film to the TD direction, and use this position as the center (hereinafter also referred to as the TD direction center), and take a width of 550 mm in each of two directions along the TD direction, and a width of 1100 mm. TD direction center of the film, 500mm position in any one of the TD directions (A direction) from the center of the TD direction, 500mm position in the TD direction opposite to the A direction (B direction) from the center of the TD direction 3 points were performed 5 times each, and the average value of 15 values was set as the stress at the time of 10% stretching in the MD direction of the film at 150 ° C. From the viewpoint of moldability and dimensional stability, the stress at 10% stretching in the MD direction of a film at 150 ° C. is more preferably 6 MPa to 20 MPa, and most preferably 7 MPa to 15 MPa.

於本發明之雙軸配向聚酯薄膜中,作為使在150℃的薄膜之MD方向之10%伸張時應力成為上述範圍 之方法,並沒有特別限定,但例如作為構成本發明之聚酯薄膜的二醇成分,含有60莫耳%以上的乙二醇成分,較佳為包含二乙二醇成分、1,3-丙二醇成分、1,4-丁二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分的至少1種類以上之二醇成分。其中,較佳為包含二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分之至少1種類以上。又,作為構成本發明之聚酯薄膜的二羧酸成分,含有60莫耳%以上的對苯二甲酸成分,較佳為包含間苯二甲酸成分、2,6-萘二羧酸成分的至少1種類以上之二羧酸成分。 In the biaxially oriented polyester film of the present invention, the stress at the time of 10% stretching in the MD direction of the film at 150 ° C is within the above range. The method is not particularly limited, but, for example, as the diol component constituting the polyester film of the present invention, it contains an ethylene glycol component of 60 mol% or more, and preferably contains a diethylene glycol component and 1,3-propanediol. Component, a 1,4-butanediol component, a 1,4-cyclohexanedimethanol component, and a diol component of at least one type of neopentyl glycol component. Among them, it is preferable to include at least one type of a diethylene glycol component, a 1,4-cyclohexanedimethanol component, and a neopentyl glycol component. The dicarboxylic acid component constituting the polyester film of the present invention contains at least 60 mol% of a terephthalic acid component, and preferably contains at least an isophthalic acid component and a 2,6-naphthalenedicarboxylic acid component. 1 or more types of dicarboxylic acid components.

於本發明之雙軸配向聚酯薄膜中,作為使在 150℃的薄膜MD方向10%伸張時應力成為上述範圍之特佳構成,較佳為於二醇成分中,含有85莫耳%以上且少於97莫耳%的乙二醇成分,含有3莫耳%以上且少於15莫耳%的二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分之至少1種類以上,於二羧酸成分中,85莫耳%以上為對苯二甲酸成分。更佳為:於二醇成分中,含有90莫耳%以上且少於95莫耳%的乙二醇成分,含有5莫耳%以上且少於10莫耳%的二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分之至少1種類以上;於二羧酸成分中,90莫耳%以上為對苯二甲酸成分,尤佳為二羧酸成分的95莫耳%以上係對苯二甲酸成分。 In the biaxially oriented polyester film of the present invention, as When the film at 150 ° C is stretched at 10% in the MD direction, the stress is in the above-mentioned range. It is preferable that the diol component contains 85 mol% or more and less than 97 mol% of the ethylene glycol component, and contains 3 mol. 1% or more of diethylene glycol component, 1,4-cyclohexanedimethanol component, neopentyl glycol component or more, at least 1 mole%, and 85 mole% of dicarboxylic acid component The above is a terephthalic acid component. More preferably, the diol component contains 90 mol% or more and less than 95 mol% of the ethylene glycol component, 5 mol% or more and less than 10 mol% of the diethylene glycol component, 1 At least one species of 4-cyclohexanedimethanol component and neopentyl glycol component; 90% or more of the dicarboxylic acid component is terephthalic acid component, and more preferably 95% of the dicarboxylic acid component Ears above% are terephthalic acid.

又,於本發明之雙軸配向聚酯薄膜中,為了 使在150℃的薄膜MD方向10%伸張時應力成為上述範圍,上述組成更佳為在薄膜兩面的面配向係數之中,高者 的面配向係數為0.111以上0.17以下。 Moreover, in the biaxially oriented polyester film of the present invention, The stress is made into the above-mentioned range when the film is stretched at 10% in the MD direction at 150 ° C, and the composition is more preferably the higher of the surface alignment coefficients on both sides of the film. The surface alignment coefficient is 0.111 or more and 0.17 or less.

使於薄膜兩面的面配向係數之中,高者的面 配向係數成為0.111以上0.17以下之方法,並沒有特別限定,但例如作為上述組成,可舉出延伸成面倍率9.8倍以上13.5倍以下之方法。又,延伸溫度較佳為70℃以上150℃以下,而且雙軸延伸後的熱處理溫度係最高溫的溫度較佳為200℃以上240℃以下。 The higher of the surface alignment coefficients on both sides of the film The method for setting the alignment coefficient to 0.111 or more and 0.17 or less is not particularly limited. For example, as the composition, a method of stretching to a surface magnification of 9.8 to 13.5 times may be mentioned. The elongation temperature is preferably 70 ° C. or higher and 150 ° C. or lower, and the heat treatment temperature after biaxial stretching is preferably the highest temperature of 200 ° C. or higher and 240 ° C. or lower.

另外,本發明之雙軸配向聚酯薄膜,係在 150℃的薄膜MD方向之熱收縮率必須為5%以下。此處,所謂在150℃的MD方向之熱收縮率,就是指將薄膜在MD方向中切出成長度150mm×寬度10mm之矩形的樣品上,以100mm之間隔描繪標線(自中央部起往兩端50mm之位置),吊掛3g的秤錘,於經加熱至150℃的熱風烘箱內放置30分鐘進行加熱處理前後的標線間距離之變化率。再者,評價係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,在1100mm寬度之薄膜的TD方向中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反的方向(B方向)之500mm之位置的3點,各自進行5次,將其15個之值的平均值設為在150℃的薄膜MD方向之熱收縮率。本發明之雙軸配向聚酯薄膜,係藉由使MD方向的150℃之熱收縮率成為5%以下,而在薄膜上塗布硬塗層、裝飾層、相位差層等的機能性塗膜,施予乾燥之際,可抑制因薄膜收縮所造成的塗膜之機能性降低、薄膜的 平面性降低等之不良狀況。MD方向的150℃之熱收縮率若為4%以下則更佳,若為3%以下則最佳。 In addition, the biaxially oriented polyester film of the present invention is The thermal shrinkage of the film in the MD direction at 150 ° C must be 5% or less. Here, the thermal shrinkage in the MD direction at 150 ° C means that the film is cut into a rectangular sample having a length of 150 mm by a width of 10 mm in the MD direction, and a reticle is drawn at an interval of 100 mm (from the center) (50mm at both ends), hang a 3g scale weight, and place it in a hot air oven heated to 150 ° C for 30 minutes before and after the heat treatment to change the distance between the marked lines. In addition, the evaluation is to set the main alignment axis direction of the arbitrary position of the film to the TD direction, and use this position as the center (hereinafter also referred to as the TD direction center), and take a width of 550 mm in each of two directions along the TD direction, and a width of 1100 mm. 3 points of the center of the TD direction of the film, a position of 500 mm in any one direction (A direction) from the center, and a position of 500 mm in the direction opposite to the A direction (B direction) from the center, Each of them was performed 5 times, and the average value of 15 values was set as the thermal shrinkage rate of the film MD direction at 150 degreeC. The biaxially oriented polyester film of the present invention is a functional coating film such as a hard coat layer, a decorative layer, a retardation layer, etc., by applying a thermal shrinkage of 150 ° C in the MD direction to 5% or less. When drying is performed, it is possible to suppress the decrease in the function of the coating film caused by the shrinkage of the film, Deterioration such as flatness. The thermal shrinkage at 150 ° C in the MD direction is more preferably 4% or less, and more preferably 3% or less.

作為使在150℃的MD方向之熱收縮率成為 5%以下之方法,可舉出例如調整雙軸延伸後的薄膜之熱處理條件之方法。藉由使處理溫度成為高溫,進行配向緩和,熱收縮率有減低之傾向,但從尺寸安定性、薄膜之品質之觀點來看,雙軸延伸後的熱處理溫度若為200℃~240℃則較佳,若為210℃~235℃則更佳,若為215℃~230℃則最佳。再者,本發明之雙軸配向聚酯薄膜的熱處理溫度,係可在差示掃描型熱量計(DSC),於氮氣環境下,以20℃/分鐘之升溫速度測定時的DSC曲線中,自起因於熱經歷的微小吸熱峰來求得。 The heat shrinkage rate in the MD direction at 150 ° C is As a method of 5% or less, the method of adjusting the heat treatment conditions of the film after biaxial stretching is mentioned, for example. By increasing the processing temperature to reduce the orientation, the thermal shrinkage tends to decrease. However, from the viewpoint of dimensional stability and film quality, the heat treatment temperature after biaxial stretching is 200 ° C to 240 ° C. Preferably, it is more preferably 210 ° C to 235 ° C, and most preferably 215 ° C to 230 ° C. In addition, the heat treatment temperature of the biaxially oriented polyester film of the present invention can be measured in a DSC curve of a differential scanning calorimeter (DSC) in a nitrogen environment at a temperature increase rate of 20 ° C / min. It is obtained by a small endothermic peak due to thermal history.

又,較佳的熱處理時間係可在5~60秒中任意 地設定,但從成型性、尺寸安定性、色調、生產性之觀點來看,較佳為10~40秒,更佳為15~30秒。另外,熱處理係藉由在長度方向及/或寬度方向中邊弛緩邊進行,可減低熱收縮率。於熱處理時使弛緩之際的弛緩率(鬆弛率)較佳為1%以上,從尺寸安定性、生產性之觀點來看,若為1%以上10%以下則較佳,若為1%以上5%以下則最佳。 In addition, the preferred heat treatment time can be arbitrarily selected from 5 to 60 seconds. From the viewpoint of moldability, dimensional stability, color tone, and productivity, it is preferably 10 to 40 seconds, and more preferably 15 to 30 seconds. In addition, the heat treatment is performed while relaxing in the longitudinal direction and / or the width direction, so that the thermal shrinkage can be reduced. The relaxation rate (relaxation rate) at the time of relaxation during heat treatment is preferably 1% or more. From the viewpoint of dimensional stability and productivity, it is preferably 1% or more and 10% or less, and 1% or more. Less than 5% is best.

另外,於2階段以上之條件下熱處理之方法亦 非常佳。於200℃~240℃之高溫下的熱處理後,在比熱處理溫度低之溫度下,於長度方向及/或寬度方向邊弛緩邊熱處理,可更減低熱收縮率。此時的第2階段之熱處理溫度較佳為120℃~低於200℃,更佳為150℃~180℃。 In addition, the method of heat treatment under the conditions of more than 2 steps is also Very good. After heat treatment at a high temperature of 200 ° C to 240 ° C, at a temperature lower than the heat treatment temperature, heat treatment is performed while relaxing in the length direction and / or width direction, which can further reduce the thermal shrinkage rate. The heat treatment temperature in the second stage at this time is preferably 120 ° C to less than 200 ° C, and more preferably 150 ° C to 180 ° C.

本發明之雙軸配向聚酯薄膜,從物性均勻性 之觀點來看,1000mm寬度的薄膜之配向角(主配向軸與薄膜TD方向或薄膜MD方向所成之角度中小者的角度)的最大值必須為20°以下。此處,所謂1000mm寬度的薄膜之配向角的最大值,就是將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心,沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜,於自該任意之點往TD方向兩端(一方為A方向,另一方為B方向)50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm(1000mm寬度)之位置,測定配向角(21點),求得其中之最大值。 The biaxially oriented polyester film of the present invention has uniform physical properties. From a viewpoint, the maximum value of the alignment angle of the film with a width of 1000 mm (the smaller of the angles formed by the main alignment axis and the film TD direction or the film MD direction) must be 20 ° or less. Here, the maximum value of the alignment angle of a film having a width of 1000 mm is to set the main alignment axis direction of an arbitrary position of the film to the TD direction, and use this position as the center to take a width of 550 mm in each of the two directions along the TD direction to make For a film with a width of 1100mm, from this arbitrary point to both ends of the TD direction (one is the A direction and the other is the B direction) 50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 450mm, 500mm (1000mm Width), the alignment angle (21 o'clock) is measured, and the maximum value is obtained.

從各自寬度方向物性均勻性之觀點來看, 1000mm寬度的薄膜之配向角的最大值若為15°以下則更佳,若為10°以下則最佳。 From the viewpoint of uniformity of physical properties in the respective width directions, The maximum value of the alignment angle of a film having a width of 1000 mm is preferably 15 ° or less, and more preferably 10 ° or less.

此處,使1000mm寬度的薄膜之配向角的最大 值成為20°以下之方法,並沒有特別限定,惟,可舉出例如使薄膜製膜中的拱起(bowing)減低之方法。具體而言,於寬度方向延伸後,一旦冷卻至聚酯之玻璃轉移溫度以下後,進行熱處理之方法,於寬度方向延伸後設置夾輥(niproll)之方法,將寬度方向的延伸分成複數區,階段地升溫之方法,將熱處理分成複數區,階段地升溫‧降溫之方法,於寬度方向中設置溫度分布,導引至熱處理區之方法,於熱處理室中亦在寬度方向中微延伸之方法等。 Here, the maximum alignment angle of a film having a width of 1000 mm is maximized. The method for the value to be 20 ° or less is not particularly limited, but examples thereof include a method for reducing bowing in film formation. Specifically, after extending in the width direction, once it is cooled to below the glass transition temperature of the polyester, heat treatment is performed, and a method of setting a nip roll after extending in the width direction to divide the extension in the width direction into a plurality of regions. The method of stepwise heating, dividing the heat treatment into multiple zones, the method of stepwise heating and cooling, setting the temperature distribution in the width direction, and guiding to the heat treatment zone, and the method of slightly extending in the width direction in the heat treatment chamber, etc. .

又,本發明之雙軸配向聚酯薄膜,從在薄膜 上塗布硬塗層、裝飾層、相位差層等之機能性塗膜,施予乾燥之際的塗膜之機能性確保、薄膜平面性確保之觀點來看,在190℃的薄膜MD方向與TD方向之熱收縮率較佳為5%以下。由於即使為190℃之高溫,也降低薄膜MD方向、TD方向之熱收縮率,故在需要將機能性塗膜的乾燥溫度予以高溫化時,也可確保高的尺寸安定性。 The biaxially oriented polyester film of the present invention From the viewpoint of ensuring the functional properties and film flatness of the coating film when a functional coating film such as a hard coat layer, a decorative layer, and a retardation layer is applied on drying, the MD direction and TD of the film at 190 ° C The thermal shrinkage in the direction is preferably 5% or less. Since the heat shrinkage of the MD direction and the TD direction of the film is reduced even at a high temperature of 190 ° C, when the drying temperature of the functional coating film needs to be increased, high dimensional stability can be ensured.

作為使在190℃的薄膜MD方向與TD方向之 熱收縮率成為5%以下之方法,可舉出例如與使150℃的薄膜MD方向之熱收縮率成為5%以下之方法同樣地,調整雙軸延伸後的薄膜之熱處理條件之方法。再者,較佳為使用階段地進行熱處理時的弛緩者,例如第一熱處理為230℃,第二熱處理以弛緩率3%在200℃,第三熱處理以弛緩率2%在180℃之方法。在190℃的薄膜MD方向/TD方向之熱收縮率較佳為5%以下/4%以下,若為5%以下/3%以下則最佳。 As the difference between MD direction and TD direction of the film at 190 ° C The method of making the heat shrinkage rate 5% or less includes, for example, a method of adjusting the heat treatment conditions of the biaxially stretched film in the same manner as the method of making the heat shrinkage rate of the film MD direction of 150 ° C. 5% or less. Furthermore, it is preferable to use a relaxer when performing heat treatment in stages. For example, the first heat treatment is 230 ° C, the second heat treatment is a relaxation rate of 3% at 200 ° C, and the third heat treatment is a relaxation rate of 2% at 180 ° C. The thermal shrinkage of the MD direction / TD direction of the film at 190 ° C is preferably 5% or less / 4%, and most preferably 5% or less / 3% or less.

又,本發明之雙軸配向聚酯薄膜,從在薄膜 上塗布硬塗層、裝飾層、相位差層等之機能性塗膜,施予乾燥之際的耐熱性、易成型性之觀點來看,1000mm寬度中的薄膜之藉由溫度調變DSC所求得之玻璃轉移溫度的最低溫度較佳為80℃以上110℃以下。此處,所謂1000mm寬度中的薄膜之藉由溫度調變DSC所求得之玻璃轉移溫度,就是指將薄膜任意之位置的主配向軸方向設為TD方向,以該位置作為中心,沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜,於自該任意之點起往TD方向兩端50mm、100mm、150mm、200mm 、250mm、300mm、350mm、400mm、450mm、500mm位置(1000mm寬度),測定玻璃轉移溫度,其中之最低溫度。所藉由溫度調變DSC所求得之玻璃轉移溫度,就是將薄膜在氣流環境下,於0℃至200℃之範圍以2℃/分鐘、溫度調變週期為60秒且溫度調變振幅1℃之正弦波狀進行測定,於所得之可逆成分溫度調變DSC圖的階梯狀變化部分中,藉由與JISK7121(1987)的「9.3玻璃轉移溫度之求得方式(1)中間點玻璃轉移溫度Tmg」記載之方法同樣之方法,求得玻璃轉移溫度之溫度。從耐熱性與成型性之觀點來看,藉由溫度調變DSC所求得之玻璃轉移溫度若為85℃以上110℃以下則更佳,若為85℃以上100℃以下則最佳。 The biaxially oriented polyester film of the present invention A functional coating film such as a hard coat layer, a decorative layer, and a retardation layer is applied, and from the standpoint of heat resistance and moldability at the time of drying, the thickness of a film in a 1000 mm width is determined by temperature control DSC. The minimum temperature of the obtained glass transition temperature is preferably 80 ° C or higher and 110 ° C or lower. Here, the so-called glass transition temperature of a film in a width of 1000 mm obtained by temperature-modulated DSC means that the main alignment axis direction of an arbitrary position of the film is set to the TD direction, and the position is used as the center to follow the TD Take a width of 550mm in each of the two directions to make a film with a width of 1100mm, and start from this arbitrary point to 50mm, 100mm, 150mm, and 200mm at both ends of the TD direction. , 250mm, 300mm, 350mm, 400mm, 450mm, 500mm (1000mm width), the glass transition temperature was measured, the lowest temperature among them. The glass transition temperature obtained by temperature-modulated DSC is that the film is in a gas flow environment at a range of 0 ° C to 200 ° C at 2 ° C / min, the temperature modulation period is 60 seconds, and the temperature modulation amplitude is 1 Measured in a sine wave shape at ℃, and in the stepwise change portion of the DSC diagram of the reversible component temperature modulation obtained, the method of "9.3 glass transition temperature determination method (1) with intermediate point glass transition temperature" in accordance with JIS K7121 (1987) The method described in "Tmg" is the same method, and the glass transition temperature is determined. From the viewpoint of heat resistance and moldability, the glass transition temperature obtained by temperature-modulated DSC is more preferably 85 ° C to 110 ° C, and most preferably 85 ° C to 100 ° C.

於本發明中,使1000mm寬度中的薄膜之藉由 溫度調變DSC所求得之玻璃轉移溫度的最低溫度成為80℃以上110℃以下之方法,並沒有特別限定,惟例如作為使上述在150℃的薄膜MD方向10%伸張時應力成為5MPa以上30MPa以下之較佳組成,於寬度方向延伸後的熱處理步驟中,較宜使用進行2%以上微延伸之方法。 In the present invention, the thickness of a film in a width of 1000 mm The method for the lowest temperature of the glass transition temperature obtained by temperature-modulated DSC to be 80 ° C. to 110 ° C. is not particularly limited, but for example, to make the above-mentioned film have a stress of 5 MPa to 30 MPa when the film is stretched at 10% in the MD direction at 150 ° C. For the following preferred composition, in the heat treatment step after the widthwise stretching, it is more preferable to use a method of performing micro-elongation of more than 2%.

又,本發明之雙軸配向聚酯薄膜,從在薄膜上塗布硬塗層、裝飾層、相位差層等之機能性塗膜,施予乾燥之際的塗膜之機能性確保、薄膜平面性確保及寬度方向的機能均勻性之觀點來看,較佳為滿足下述(I)式。 In addition, the biaxially oriented polyester film of the present invention has a functional coating film such as a hard coat layer, a decorative layer, a retardation layer, etc. applied to the film, and the functional film of the coating film at the time of drying is ensured and the film is flat. From the viewpoint of ensuring uniformity in the width direction, it is preferable to satisfy the following formula (I).

(SAMD+SBMD)/(SCMD×2)≦1.2 (I) (SA MD + SB MD ) / (SC MD × 2) ≦ 1.2 (I)

惟,SAMD:自1100mm寬度薄膜的TD方向之中心起,在TD方向的任意之一方向(A方向)的500mm之位置的 MD方向之190℃熱收縮率 However, SA MD : From the center of the TD direction of a 1100 mm-thick film, the thermal contraction rate at 190 ° C in the MD direction at a position of 500 mm in any one of the TD directions (A direction)

SBMD:自1100mm寬度薄膜的寬度方向之中心起,在TD方向之與A方向相反的方向(B方向)的500mm之位置的MD方向之190℃熱收縮率 SB MD : From the center of the width direction of the 1100mm width film, the thermal shrinkage rate at 190 ° C in the MD direction at a position of 500mm in the TD direction opposite to the A direction (B direction)

SCMD:在1100mm寬度薄膜的TD方向之中心的MD方向之190℃熱收縮率。 SC MD : Thermal shrinkage at 190 ° C in the MD direction at the center of the TD direction of a 1100 mm-thick film.

對於1100mm寬度薄膜(將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜)的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反的方向(B方向)之500mm之位置的3點,對於經切出成長度150mm(A方向或B方向)×寬度10mm之矩形的樣品,各自測定5次的在190℃的熱收縮率,各自之平均值。 For a film with a width of 1100 mm (the main alignment axis direction of any position of the film is set to the TD direction, and the position is used as the center (hereinafter also referred to as the TD direction center)), a width of 550 mm is taken in each of the 2 directions along the TD direction, and the width is 1100mm film) in the center of the TD direction, at a position of 500mm in any one of the TD directions (A direction) from the center, at a position of 500mm in the TD direction from the center opposite to the A direction (B direction) At three points, the thermal shrinkage at 190 ° C. was measured five times for each sample cut out into a rectangular shape having a length of 150 mm (A direction or B direction) × width of 10 mm, and the respective average values were obtained.

滿足(I)式者,就是表示1000mm寬度薄膜的TD方向之MD熱收縮率之差小,可抑制在薄膜上塗布機能性塗膜並施予乾燥之際的方向之機能性塗膜的不均、薄膜之不均。從TD方向物性均勻性之觀點來看,更佳為滿足(I)’式,最佳為滿足(I)”式。 If the formula (I) is satisfied, it means that the difference in MD thermal shrinkage in the TD direction of a film with a width of 1000 mm is small, and the unevenness of the functional coating film in the direction when the functional coating film is applied to the film and dried is suppressed. , Uneven film. From the viewpoint of uniformity of the physical properties in the TD direction, it is more preferable to satisfy the formula (I) ', and it is more preferable to satisfy the formula (I) ".

(SAMD+SBMD)/SCMD×2≦1.15 (I)’ (SA MD + SB MD ) / SC MD × 2 ≦ 1.15 (I) '

(SAMD+SBMD)/SCMD×2≦1.1 (I)” (SA MD + SB MD ) / SC MD × 2 ≦ 1.1 (I) ”

本發明之雙軸配向聚酯薄膜滿足(I)式之方法並沒有特別限定,但使上述之1000mm寬度的薄膜之配向角的最大值成為20°以下。 The method for satisfying the formula (I) of the biaxially oriented polyester film of the present invention is not particularly limited, but the maximum value of the alignment angle of the above-mentioned film having a width of 1000 mm becomes 20 ° or less.

再者,使於熱機械分析(TMA)中,以19.6mN 的荷重,自25℃至200℃為止以5℃/分鐘的升溫速度升溫時之薄膜MD方向的伸張尖峰溫度成為60℃以上者亦有效。此處,所謂薄膜MD方向的伸張尖峰溫度,就是指隨著升溫進行伸張的薄膜轉移至收縮行為的溫度。薄膜一旦收縮後,亦有再度轉移至伸張行為的情況,但於本發明中,將自25℃至200℃為止升溫時的最初由伸張行為轉移至收縮行為的溫度設為薄膜MD方向的伸張尖峰溫度。測定係對於1100mm寬度薄膜(將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,作為1100mm寬度之薄膜)的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反之方向(B方向)之500mm之位置的3點,各自在MD、TD皆各進行3次,採用對於MD、TD所測定的9個值之平均值。為了使以19.6mN的荷重,自25℃至200℃為止以5℃/分鐘的升溫速度升溫時之薄膜長度方向的伸張尖峰溫度成為60℃以上,將薄膜製膜時的長度方向之延伸倍率設定在2.8倍~3.4倍,較佳2.9~3.3倍者係有效。作為薄膜的延伸倍率,雖然沒有特別的條件,但發明者們進行各種的檢討,結果發現藉由使薄膜的長度方向之延伸倍率成為上述範圍,可特別地使以19.6mN的荷重,自25℃至200℃為止以5℃/分鐘的升溫速度升溫時之薄膜長度方向的伸張尖峰溫度成為60℃以上。 In addition, the thermomechanical analysis (TMA) was performed at 19.6 mN. It is also effective that the stretch peak temperature in the MD direction of the film when the temperature rises from 25 ° C to 200 ° C at a temperature increase rate of 5 ° C / min becomes 60 ° C or higher. Here, the stretching peak temperature in the MD direction of the film refers to a temperature at which the stretched film transitions to a shrinking behavior as the temperature increases. Once the film shrinks, it may shift to the stretching behavior again. However, in the present invention, the temperature at which the transition from the stretching behavior to the shrinking behavior is initially set as the stretching peak in the MD direction of the film when the temperature rises from 25 ° C to 200 ° C. temperature. The measurement system is for a 1100 mm wide film (the main alignment axis direction of any position of the film is set to the TD direction, and the position is used as the center (hereinafter also referred to as the TD direction center)). Film with a width of 1100 mm) in the center of the TD direction, at a position of 500 mm in any one of the TD directions (A direction) from the center, at a position of 500 mm in the TD direction from the center (direction B) For each of the three points, three times were performed in MD and TD, and the average of the nine values measured for MD and TD was used. In order to increase the stretching peak temperature in the length direction of the film when the temperature is increased from 25 ° C to 200 ° C and a temperature increase rate of 5 ° C / min from 25 ° C to 200 ° C, the stretching rate in the lengthwise direction during film formation is set Effective from 2.8 to 3.4 times, preferably from 2.9 to 3.3 times. Although there are no special conditions for the stretch ratio of the film, the inventors conducted various reviews and found that by setting the stretch ratio in the longitudinal direction of the film to be in the above range, it is possible to specifically set the stretch ratio to 25 ° C under a load of 19.6 mN. When the temperature was raised up to 200 ° C at a temperature increase rate of 5 ° C / min, the stretching peak temperature in the longitudinal direction of the film became 60 ° C or higher.

又,本發明之雙軸配向聚酯薄膜較佳為滿足下述(II)式。 The biaxially oriented polyester film of the present invention preferably satisfies the following formula (II).

(SATD+SBTD)/SCTD×2≦1.2 (II) (SA TD + SB TD ) / SC TD × 2 ≦ 1.2 (II)

惟,SATD:自1100mm寬度薄膜(將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,作為1100mm寬度之薄膜)的TD方向之中心起,在TD方向的任意之一方向(A方向)的500mm之位置的TD方向之190℃熱收縮率 However, SA TD : From the 1100mm width film (the main alignment axis direction of any position of the film is set to the TD direction, with this position as the center (hereinafter also referred to as the TD direction center), 550mm in each of the 2 directions along the TD direction Width, as the center of the TD direction of a film with a width of 1100 mm), at a temperature of 190 ° C in the TD direction at a position of 500 mm in any one of the TD directions (A direction)

SBTD:自1100mm寬度薄膜的TD方向之中心起,在TD方向之與A方向相反的方向(B方向)的500mm之位置的TD方向之190℃熱收縮率 SB TD : From the center of the TD direction of a 1100mm wide film, the thermal shrinkage of 190 ° C in the TD direction at a position of 500mm in a direction opposite to the A direction (B direction)

SCTD:在1100mm寬度薄膜的TD方向之中心的TD方向之190℃熱收縮率。 SC TD : Thermal shrinkage of 190 ° C in the TD direction at the center of the TD direction of a 1100 mm-thick film.

滿足(II)式者,就是表示1000mm寬度薄膜的TD方向之TD熱收縮率之差小,可抑制在薄膜上塗布機能性塗膜並施予乾燥之際的方向之機能性塗膜的不均、薄膜之不均。從TD方向物性均勻性之觀點來看,更佳為滿足(II)’式,最佳為滿足(II)”式。 If the formula (II) is satisfied, it means that the difference in TD thermal shrinkage in the TD direction of a film having a width of 1000 mm is small, and the unevenness of the functional coating film in the direction when the functional coating film is applied to the film and dried is suppressed. , Uneven film. From the viewpoint of uniformity of the physical properties in the TD direction, it is more preferable to satisfy the formula (II) ', and it is more preferable to satisfy the formula (II) ".

(SATD+SBTD)/SCTD×2≦1.15 (II)’ (SA TD + SB TD ) / SC TD × 2 ≦ 1.15 (II) '

(SATD+SBTD)/SCTD×2≦1.1 (II)” (SA TD + SB TD ) / SC TD × 2 ≦ 1.1 (II) ”

本發明之雙軸配向聚酯薄膜滿足(II)式之方法並沒有特別限定,但使上述之1000mm寬度的薄膜之配向角的最大值成為20°以下。再者,使於熱機械分析(TMA)中,以19.6mN的荷重,自25℃至200℃為止以5℃/分鐘的升溫 速度升溫時之膜TD方向的伸張尖峰溫度成為70℃以上,而變得容易滿足(II)式。此處,所謂薄膜TD方向的伸張尖峰溫度,就是指隨著升溫進行伸張的薄膜轉移至收縮行為的溫度。測定係對於1100mm寬度薄膜(將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(以下亦稱為TD方向中心),沿著TD方向於2方向各自取550mm寬度,作為1100mm寬度之薄膜)的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反之方向(B方向)之500mm之位置的3點,各自在MD、TD皆各進行3次,採用對於MD、TD所測定的9點之平均值。薄膜一旦收縮後,亦有再度轉移至伸張行為的情況,但於本發明中,將自25℃至200℃為止升溫時的最初由伸張行為轉移至收縮行為的溫度當作膜TD方向的伸張尖峰溫度。為了使於熱機械分析(TMA)中,以19.6mN的荷重,自25℃至200℃為止以5℃/分鐘的升溫速度升溫時之薄膜TD方向的伸張尖峰溫度成為70℃以上,將製膜時的長度方向之延伸倍率設定在2.8倍~3.4倍之方法,更且強化寬度方向延伸後的熱處理步驟之微延伸者係有效。 The method for satisfying the formula (II) of the biaxially oriented polyester film of the present invention is not particularly limited, but the maximum value of the alignment angle of the film having a width of 1000 mm described above is 20 ° or less. In addition, in a thermomechanical analysis (TMA), a temperature of 5 ° C / min was raised from 25 ° C to 200 ° C under a load of 19.6mN. The stretching peak temperature of the film in the TD direction at the time of temperature increase becomes 70 ° C. or higher, and it becomes easy to satisfy the formula (II). Here, the stretch peak temperature in the TD direction of the film refers to a temperature at which the stretched film transitions to a shrinking behavior as the temperature increases. The measurement system is for a 1100 mm wide film (the main alignment axis direction of any position of the film is set to the TD direction, and the position is used as the center (hereinafter also referred to as the TD direction center)). Film with a width of 1100 mm) in the center of the TD direction, at a position of 500 mm in any one of the TD directions (A direction) from the center, at a position of 500 mm in the TD direction from the center (direction B) Each of the three points was performed three times in MD and TD, and the average value of nine points measured for MD and TD was used. Once the film has shrunk, it may shift to the stretching behavior again. However, in the present invention, the temperature at which the transition from the stretching behavior to the shrinking behavior is initially taken as the stretching peak in the TD direction of the film when the temperature rises from 25 ° C to 200 ° C. temperature. In order to increase the peak temperature in the TD direction of the thin film during thermomechanical analysis (TMA) with a load of 19.6mN and a temperature increase rate of 5 ° C / min from 25 ° C to 200 ° C to 70 ° C or higher, the film was formed. The method of setting the stretching ratio in the length direction at the time of 2.8 times to 3.4 times is more effective, and the micro-elongator that strengthens the heat treatment step after stretching in the width direction is effective.

又,作為使本發明之雙軸配向聚酯薄膜滿足 (I)式、(II)式之方法,進行離線退火(off-annealing)者亦有效。即,對經一次捲繞的聚酯薄膜,再施予熱處理之方法。離線退火處理溫度係140℃以上200℃以下,寬度方向為自由狀態,由於寬度方向的熱收縮之差消失,而可滿足(I)式、(II)式。離線退火處理溫度較佳為150℃以 上200℃以下,最佳為160℃以上200℃以下。 In addition, as a result of satisfying the biaxially oriented polyester film of the present invention, The methods of formulas (I) and (II) are also effective for off-annealing. That is, the polyester film which has been wound once is subjected to a heat treatment method. The off-line annealing treatment temperature is 140 ° C. to 200 ° C., and the width direction is a free state. Since the difference in heat shrinkage in the width direction disappears, the formulas (I) and (II) can be satisfied. The off-line annealing treatment temperature is preferably 150 ° C or higher. Above 200 ° C, preferably 160 ° C to 200 ° C.

非常重要的是本發明之雙軸配向聚酯薄膜同 時滿足以下之物性:在150℃的薄膜MD方向之10%伸張時應力為5MPa以上30MPa以下,在150℃的薄膜MD方向之熱收縮率為5%以下,1000mm寬度的薄膜之配向角的最大值為20°以下。若欲使在150℃的薄膜MD方向之10%伸張時應力成為5MPa以上30MPa以下,則在150℃的MD方向之熱收縮率有變高之情況,而且發生難以將1000mm寬度的薄膜配向角之最大值控制在20°以下之情況。作為解決此左右為難的方法,本發明之雙軸配向聚酯薄膜較佳成為具有聚酯A層與聚酯B層之積層薄膜構成,聚酯A層係位於至少一側之最外層的構成。 It is very important that the biaxially oriented polyester film of the present invention is the same as It meets the following physical properties: 10% of the MD direction of the film at 150 ° C, the stress is 5 MPa or more and 30 MPa or less, the thermal shrinkage of the film at 150 ° C in the MD direction is less than 5%, and the maximum orientation angle of the film with a width of 1000 mm is the largest. The value is 20 ° or less. If the stress in the MD direction of a film at 150 ° C is stretched to 10 MPa or more and the stress is 5 MPa or more and 30 MPa or less, the thermal shrinkage in the MD direction at 150 ° C may become high, and it may be difficult to align the film with a film width of 1,000 mm. When the maximum value is controlled below 20 °. As a method to solve this difficulty, the biaxially oriented polyester film of the present invention is preferably a laminated film structure having a polyester A layer and a polyester B layer, and the polyester A layer is the outermost layer on at least one side.

於本發明中,當為具有聚酯A層與聚酯B層之積層薄膜時,熔點高者之層為聚酯A層。 In the present invention, when the laminated film has a polyester A layer and a polyester B layer, the layer having the higher melting point is the polyester A layer.

本發明之聚酯薄膜,係藉由具有熔點高的A層與熔點比A層低的B層,而A層成為剛直的層,將在150℃的薄膜MD方向之熱收縮率保持5%以下之低,更且可容易地使1000mm寬度的薄膜之配向角的最大值成為20°以下,達成滿足寬度方向的物性均勻性之任務,另一方面,B層係作為運動性高之層,可容易使在150℃的薄膜MD方向之10%伸張時應力成為5MPa以上30MPa以下,完成可達成易成形性之任務,可滿足以單膜構成所難以兼顧的特性。本發明之聚酯薄膜中的A層,從尺寸安定性、寬度方向物性均勻性之觀點來看,面配向係數若為0.111以上0.17以下則較佳,若為0.13以上0.17以下則更 佳,若為0.145以上0.17以下則最佳。 The polyester film of the present invention has an A layer having a high melting point and a B layer having a lower melting point than the A layer, and the A layer becomes a rigid layer, and the heat shrinkage rate of the film in the MD direction at 150 ° C is kept below 5%. It is low, and it is easy to make the maximum value of the alignment angle of a film with a width of 1000 mm be 20 ° or less, to achieve the task of satisfying the uniformity of physical properties in the width direction. On the other hand, layer B is a layer with high mobility, which can It is easy to make the stress at 10% of the MD direction of the film at 150 ° C to be 5 MPa or more and 30 MPa or less, and the task of achieving formability can be achieved, which can meet the characteristics that are difficult to take into consideration with a single film configuration. In the polyester film of the present invention, from the viewpoint of dimensional stability and uniformity of physical properties in the width direction, the surface alignment coefficient is preferably 0.111 or more and 0.17 or less, and more preferably 0.13 or more and 0.17 or less. It is preferably at least 0.145 and at most 0.17.

又,從薄膜的捲曲抑制之觀點來看,當本發 明之雙軸配向聚酯薄膜為具有聚酯A層與聚酯B層之積層聚酯薄膜時,較佳為A層/B層/A層之3層構成。 Also, from the viewpoint of curl suppression of the film, when the present invention When Mingzhi's biaxially oriented polyester film is a laminated polyester film having a polyester A layer and a polyester B layer, it is preferably composed of three layers of A layer / B layer / A layer.

於本發明之雙軸配向聚酯薄膜中,當為具有 聚酯A層與聚酯B層之積層薄膜時,為了同時滿足在150℃的薄膜MD方向之10%伸張時應力為5MPa以上30MPa以下、在150℃的薄膜MD方向之熱收縮率為5%以下、1000mm寬度的薄膜之配向角的最大值為20°以下之物性,作為聚酯A層、聚酯B層之較佳態樣,可舉出如下述之構成。 In the biaxially oriented polyester film of the present invention, when When a polyester A layer and a polyester B layer are laminated, in order to satisfy the 10% MD of the film at 150 ° C, the tensile stress is 5 MPa or more and 30 MPa or less, and the thermal shrinkage of the film at 150 ° C in the MD direction is 5%. Below, the maximum value of the alignment angle of a film having a width of 1000 mm is 20 ° or less. As a preferable aspect of the polyester A layer and the polyester B layer, the following configuration can be mentioned.

聚酯A層之作為二醇成分,較佳為含有90莫 耳%以上且少於99莫耳%的乙二醇成分,二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇之至少1種類以上係含有1莫耳%以上且少於10莫耳%;作為二羧酸成分,較佳為90莫耳%以上為對苯二甲酸成分。更佳為,作為二醇成分,含有95莫耳%以上且少於99莫耳%的乙二醇成分,二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分之至少1種類以上係含有1莫耳%以上且少於5莫耳%;作為二羧酸成分,95莫耳%以上為對苯二甲酸成分,更佳為於上述二醇成分中,二羧酸成分的98莫耳%以上為對苯二甲酸成分較佳。 The polyester A layer preferably contains 90 moles as a diol component. At least 1 type of ethylene glycol component, less than 99 mol%, diethylene glycol component, 1,4-cyclohexane dimethanol component, and neopentyl glycol contains at least 1 mol% and Less than 10 mole%; as the dicarboxylic acid component, preferably 90 mole% or more is a terephthalic acid component. More preferably, as the diol component, 95 mol% or more and less than 99 mol% of a glycol component, a diethylene glycol component, a 1,4-cyclohexanedimethanol component, and a neopentyl glycol component are contained. At least one type or more contains 1 mol% or more and less than 5 mol%; as a dicarboxylic acid component, 95 mol% or more is a terephthalic acid component, and more preferably, among the above diol components, dicarboxylic acid At least 98 mol% of the acid component is preferably a terephthalic acid component.

聚酯B層之作為二醇成分,較佳為含有80莫 耳%以上且少於95莫耳%的乙二醇成分,二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分之至少1種類以上 係含有5莫耳%以上且少於20莫耳%;作為二羧酸成分,較佳為90莫耳%以上為對苯二甲酸成分。更佳為,作為二醇成分,含有85莫耳%以上且少於95莫耳%的乙二醇成分,二乙二醇成分、1,4-環己烷二甲醇成分、新戊二醇成分之至少1種類以上係含有5莫耳%以上且少於15莫耳%;作為二羧酸成分係95莫耳%以上為對苯二甲酸成分,更佳為於上述二醇成分中,二羧酸成分的98莫耳%以上為對苯二甲酸成分較佳。 Polyester B layer preferably contains 80 moles as a diol component At least 1 type of ethylene glycol component, less than 95 mol%, diethylene glycol component, 1,4-cyclohexanedimethanol component, and at least one type of neopentyl glycol component It contains 5 mol% or more and less than 20 mol%; as the dicarboxylic acid component, 90 mol% or more is preferably a terephthalic acid component. More preferably, as the diol component, 85 mol% or more and less than 95 mol% of a glycol component, a diethylene glycol component, a 1,4-cyclohexanedimethanol component, and a neopentyl glycol component are contained. At least one type or more contains 5 mol% or more and less than 15 mol%; as the dicarboxylic acid component, 95 mol% or more is a terephthalic acid component, and more preferably, among the above diol components, dicarboxylic acid At least 98 mol% of the acid component is preferably a terephthalic acid component.

其次,記載本發明之雙軸配向聚酯薄膜的具體製造方法之例,惟本發明不受如此之例所限定解釋。 Next, an example of a specific manufacturing method of the biaxially-oriented polyester film of the present invention is described, but the present invention is not limited to the explanation of such an example.

成為具有聚酯A層與聚酯B層之積層聚酯薄膜時,首先作為使用於聚酯A層的聚酯A,以指定的比例計量聚對苯二甲酸乙二酯樹脂(a)與1,4-環己烷二甲醇共聚合聚對苯二甲酸乙二酯樹脂(b)。又,作為使用於聚酯B層的聚酯B,以指定的比例計量聚對苯二甲酸乙二酯樹脂(c)與1,4-環己烷二甲醇共聚合聚對苯二甲酸乙二酯樹脂(d)。 When forming a laminated polyester film having a polyester A layer and a polyester B layer, first as the polyester A used for the polyester A layer, measure the polyethylene terephthalate resin (a) and 1 at a specified ratio. , 4-cyclohexanedimethanol copolymerized polyethylene terephthalate resin (b). In addition, as the polyester B used in the polyester B layer, polyethylene terephthalate resin (c) was copolymerized with 1,4-cyclohexanedimethanol at a specified ratio to measure polyethylene terephthalate. Ester resin (d).

而且,將所混合的聚酯樹脂供給至排氣式雙軸擠壓機,進行熔融擠出。此時,較佳為擠壓機內在流通氮氣環境下,氧濃度為0.7體積%以下,將樹脂溫度控制在265℃~295℃。其次,通過過濾器或齒輪泵,分別進行異物之去除、擠出量之勻整化,經由T模頭在冷卻滾筒上吐出片狀。於該情況下,藉由使用施加有高電壓的電極,以靜電使冷卻滾筒與樹脂緊貼之靜電施加法,在澆鑄滾筒與所擠出的聚合物片間設置水膜之澆鑄法,使 澆鑄滾筒溫度成為聚酯樹脂的玻璃轉移點~(玻璃轉移點-20℃),使所擠出的聚合物黏著之方法,或複數組合有此等的方法之方法,而使片狀聚合物緊貼於澆鑄滾筒,進行冷卻固化,得到未延伸薄膜。於此等之澆鑄法中,使用聚酯時,從生產性或平面性之觀點來看,較宜使用靜電施加之方法。 Then, the mixed polyester resin was supplied to a vented biaxial extruder and melt-extruded. At this time, it is preferable to control the resin temperature at 265 ° C to 295 ° C in an extruder under an atmosphere of flowing nitrogen, with an oxygen concentration of 0.7% by volume or less. Next, a filter or a gear pump is used to remove foreign matter and homogenize the amount of extrusion, respectively, and spit out a sheet on a cooling drum through a T die. In this case, by using an electrostatic application method in which an electrode to which a high voltage is applied and the cooling roller and the resin are brought into close contact with each other by static electricity, a casting method in which a water film is provided between the casting roller and the extruded polymer sheet is used. The method of casting the roller temperature to the glass transition point of polyester resin (glass transition point -20 ° C), the method of making the extruded polymer adhere, or a combination of these methods, to make the sheet polymer tight. It was affixed to a casting drum and cooled and solidified to obtain an unstretched film. Among these casting methods, when polyester is used, a method of applying static electricity is more preferable from the viewpoint of productivity or flatness.

本發明之雙軸配向聚酯薄膜,從耐熱性、尺 寸安定性之觀點來看,必須成為雙軸配向薄膜。雙軸配向薄膜係可藉由將未延伸薄膜在長度方向中延伸後,於寬度方向中延伸,或在寬度方向中延伸後,於長度方向中延伸之逐次雙軸延伸方法,或藉由幾乎同時地在薄膜之長度方向、寬度方向中延伸之同時雙軸延伸方法等,進行延伸而得。 The biaxially oriented polyester film of the present invention From the viewpoint of inch stability, it must be a biaxial alignment film. The biaxially oriented film can be a sequential biaxially stretching method in which the unstretched film is stretched in the lengthwise direction and then in the widthwise direction, or after being stretched in the widthwise direction and in the lengthwise direction, or by almost simultaneously It can be obtained by performing a biaxial stretching method while simultaneously extending the ground in the length direction and the width direction of the film.

作為該延伸方法中的延伸倍率,於長度方向中較佳為採用2.8倍以上3.4倍以下,更佳採用2.9倍以上3.3倍以下。又,延伸速度宜為1,000%/分鐘以上200,000%/分鐘以下。另外,長度方向之延伸溫度較佳為70℃以上90℃以下。還有,寬度方向之延伸倍率較佳採用3.1倍以上4.5倍以下,更佳採用3.5倍以上4.2倍以下。寬度方向之延伸速度宜為1,000%/分鐘以上200,000%/分鐘以下。又,為了一邊使在150℃的薄膜MD方向之10%伸張時應力成為5MPa以上30MPa以下,一邊使1000mm寬度的薄膜之配向角的最大值成為20°以下,較佳為寬度方向的延伸係分成複數區,邊階段地升溫邊延伸之方法,可舉出例如於延伸前半溫度為90℃以上120℃以下,延伸中途溫度為 100℃以上130℃以下,更且延伸後半溫度為110℃以上150℃以下,依延伸前半溫度、延伸中途溫度、延伸後半溫度之順序提高溫度之方法。 As the stretching magnification in this stretching method, it is preferable to use 2.8 times to 3.4 times in the longitudinal direction, and it is more preferable to use 2.9 times to 3.3 times. The elongation speed is preferably 1,000% / minute or more and 200,000% / minute or less. The stretching temperature in the longitudinal direction is preferably 70 ° C or higher and 90 ° C or lower. The stretching ratio in the width direction is preferably 3.1 times to 4.5 times, and more preferably 3.5 times to 4.2 times. The extension speed in the width direction is preferably 1,000% / minute or more and 200,000% / minute or less. In addition, in order to make the maximum value of the alignment angle of a film having a width of 1,000 mm to 20 ° or less while the stress at a stretch of 10% in the MD direction of the film at 150 ° C. is 5 MPa to 30 MPa, the extension system in the width direction is preferably divided The method of stretching in a plurality of zones while gradually heating up includes, for example, a temperature of 90 ° C or higher and 120 ° C or lower during the first half of stretching, and 100 ° C or higher and 130 ° C or lower, and the second half stretching temperature is 110 ° C or higher and 150 ° C or lower, the method is to increase the temperature in the order of the first half of the temperature, the temperature during the middle of the stretching, and the second half of the stretching.

再者,於雙軸延伸之後進行薄膜的熱處理。 熱處理係可在烘箱中,於經加熱的輥上等,藉由習知的任意方法進行。此熱處理係在120℃以上且聚酯的結晶熔解尖峰溫度以下之溫度進行,惟較佳為200℃以上240℃以下,更佳為210℃~235℃,最佳為215℃~230℃。在此所謂的較佳熱處理溫度,就是表示在雙軸延伸後所進行的熱處理溫度之中,成為最高溫之溫度。又,熱處理時間係在不使特性惡化的範圍中可為任意,較佳為5秒以上60秒以下,更佳為10秒以上40秒以下,最佳可以15秒以上30秒以下進行。另外,為了一邊使在150℃的薄膜MD方向之10%伸張時應力成為5MPa以上30MPa以下,使在150℃的薄膜MD方向之熱收縮率成為5%以下,一邊使1000mm寬度的薄膜之配向角的最大值成為20°以下,較宜採用將熱處理分成複數區,階段地升溫‧降溫之方法,或於熱處理步驟中在寬度方向中微延伸之方法。可舉出例如使熱處理前半溫度為180℃以上210℃以下,在寬度方向中微延伸1%以上10%以下,較佳3%以上10%以下,使熱處理中途溫度為200℃以上240℃以下,在寬度方向中微延伸1%以上10%以下,較佳3%以上10%以下,使熱處理後半溫度為150℃以上且低於200℃之方法。熱處理後半溫度,為了降低熱收縮率,邊弛緩1%以上10%以下邊實施亦較佳。再者,為了提高與印刷層或接著劑、 蒸鍍層、硬塗層、耐候層等的各種加工層之接著力,亦可至少對單面進行電暈處理,塗覆易接著層。作為在薄膜製程內之線內設置塗層之方法,較佳為在已進行至少單軸延伸的薄膜上,使用計量環形棒(metering ring bar)或凹槽輥等,均勻地塗布在水中分散有塗層組成物者,邊施予延伸邊使塗劑乾燥之方法,於該情況下,易接著層厚度較佳為0.01μm以上1μm以下。又,於易接著層中亦可添加各種添加劑,例如抗氧化劑、耐熱安定劑、紫外線吸收劑、紅外線吸收劑、顏料、染料、有機或無機粒子、抗靜電劑、核劑等。作為易接著層所較宜使用的樹脂,從接著性、操作性之方面來看,較佳為由丙烯酸樹脂、聚酯樹脂及胺基甲酸酯樹脂中選出的至少1種樹脂。再者,亦較宜使用在140~200℃條件下進行離線退火者。 After the biaxial stretching, the film is heat-treated. The heat treatment can be performed in an oven, on a heated roll, or the like, by any conventional method. This heat treatment is performed at a temperature of 120 ° C or higher and below the crystal melting peak temperature of the polyester, but preferably 200 ° C to 240 ° C, more preferably 210 ° C to 235 ° C, and most preferably 215 ° C to 230 ° C. The so-called preferred heat treatment temperature means the highest temperature among the heat treatment temperatures performed after biaxial stretching. The heat treatment time may be arbitrarily selected within a range that does not deteriorate the characteristics, preferably 5 seconds or more and 60 seconds or less, more preferably 10 seconds or more and 40 seconds or less, and most preferably 15 seconds or more and 30 seconds or less. In addition, the orientation angle of a film having a width of 1000 mm was set to make the thermal shrinkage of the film in the MD direction at 150 ° C less than 5% while the stress in the MD direction of the film being stretched at 10% at 150 ° C was 5 MPa to 30 MPa. The maximum value is less than 20 °. It is more appropriate to use a method of dividing the heat treatment into multiple zones and gradually raising and lowering the temperature, or a method of slightly extending in the width direction during the heat treatment step. For example, the temperature before the heat treatment can be 180 ° C or higher and 210 ° C or lower, and slightly stretched in the width direction by 1% or higher and 10% or lower, preferably 3% or higher and 10% or lower. A method of slightly extending in the width direction by 1% or more and 10% or less, preferably 3% or more and 10% or less, so that the half temperature after the heat treatment is 150 ° C or more and 200 ° C or less. At the half temperature after the heat treatment, in order to reduce the thermal shrinkage, it is also preferable to carry out while relaxing 1% to 10%. Moreover, in order to improve the printing layer or adhesive, The adhesion of various processed layers, such as a vapor-deposited layer, a hard coat layer, and a weather-resistant layer, can also be corona-treated on at least one side to apply an easy-adhesive layer. As a method for providing a coating in a line in a film manufacturing process, it is preferable to uniformly coat the film that has been subjected to at least uniaxial stretching with a metering ring bar or a grooved roller and disperse it in water. In the case of a coating composition, the method of drying the coating agent while applying extension is preferable. In this case, the thickness of the easy-adhesive layer is preferably 0.01 μm or more and 1 μm or less. Various additives such as an antioxidant, a heat-resistant stabilizer, an ultraviolet absorber, an infrared absorber, a pigment, a dye, organic or inorganic particles, an antistatic agent, and a nucleating agent may be added to the easy-adhesive layer. As the resin preferably used for the easy-adhesion layer, at least one resin selected from the group consisting of acrylic resin, polyester resin, and urethane resin is preferred from the viewpoint of adhesiveness and handling properties. Furthermore, it is more suitable to use offline annealing at 140 ~ 200 ℃.

本發明之雙軸配向聚酯薄膜,由於在150℃的 成型應力低,而易成型性良好,且由於150℃之熱收縮率低,而塗布乾燥時的薄膜變形小,更且由於1000mm寬度的薄膜之最大配向角小,寬度方向之物性均勻性優異,可適用於建材、行動機器、電機製品、汽車零件、遊戲機零件等之成型裝飾用途、或偏光板等的光學用薄膜等之連工程薄膜一起施予成型的成型加工用途。其中,由於寬度方向的物性均勻性非常優異,較宜使用在光學用途,具體而言為了達成相位差層之高精細化、薄膜化,在工程薄膜上塗布相位差層,連工程薄膜一起成型之用途。 The biaxially oriented polyester film of the present invention Low molding stress and good moldability. Due to the low thermal shrinkage at 150 ° C, the film deformation during coating and drying is small, and because the maximum alignment angle of a film with a width of 1000 mm is small, the physical properties in the width direction are excellent. It is suitable for molding and processing applications such as building materials, mobile equipment, motor products, automobile parts, game machine parts, and other decorative films, or optical films such as polarizing plates. Among them, since the uniformity of the physical properties in the width direction is very excellent, it is more suitable for optical applications. Specifically, in order to achieve high definition and thin film of the retardation layer, the retardation layer is coated on the engineering film, and the engineering film is molded together. use.

[實施例] [Example]

(1)聚酯之組成 (1) Composition of polyester

可將聚酯樹脂及薄膜溶解於六氟異丙醇(HFIP)中,使用1H-NMR及13C-NMR來定量各單體殘基成分或副生成二乙二醇之含量。於積層薄膜時,可按照積層厚度,削取薄膜的各層,採集構成各層單質之成分,進行評價。再者,對於本發明之薄膜,藉由自薄膜製造時的混合比率來計算,而算出組成。 Polyester resin and film can be dissolved in hexafluoroisopropanol (HFIP), and the content of each monomer residue component or by-product diethylene glycol can be quantified using 1 H-NMR and 13 C-NMR. When laminating a film, each layer of the film can be cut out according to the thickness of the layer, and the components constituting each element of the layer can be collected and evaluated. The composition of the film of the present invention is calculated from the mixing ratio at the time of film production.

(2)聚酯之固有黏度 (2) inherent viscosity of polyester

聚酯樹脂及薄膜之極限黏度,係將聚酯溶解於鄰氯苯酚中,使用奧士瓦黏度計在25℃測定。於積層薄膜時,可按照積層厚度,削取薄膜的各層,評價各層單質的固有黏度。 The limiting viscosity of polyester resins and films is that polyester is dissolved in o-chlorophenol and measured at 25 ° C using an Oshwa viscosity meter. When the film is laminated, each layer of the film can be cut out according to the thickness of the laminate, and the inherent viscosity of each element of the layer can be evaluated.

(3)薄膜厚度、層厚度 (3) film thickness, layer thickness

將薄膜包埋於環氧樹脂中,用切片機切出薄膜截面。用透射型電子顯微鏡(日立製作所製TEM H7100),以5000倍之倍率觀察該截面,求得薄膜厚度及聚酯層之厚度。 The film was embedded in epoxy resin, and the cross section of the film was cut out with a microtome. The cross section was observed with a transmission electron microscope (TEM H7100 manufactured by Hitachi, Ltd.) at a magnification of 5000 times, and the thickness of the film and the thickness of the polyester layer were determined.

(4)熔點 (4) Melting point

使用差示掃描熱量計(SEIKO電子工業製RDC220),依據JIS K7121-1987、JIS K7122-1987,進行測定及解析。於樣品中使用5mg聚酯薄膜,將藉由自25℃起以20℃/分鐘升溫至300℃為止時的DSC曲線所得之吸熱峰的頂點之溫度設為熔點。再者,於積層薄膜時,可按照積層厚度,削取薄膜的各層,測定各層單質之熔點。於本發 明中,當為具有聚酯A層與聚酯B層的積層聚酯薄膜之情況,測定各層之熔點,將熔點高的層設為聚酯A層,將低者的層設為聚酯B層。 Measurement and analysis were performed using a differential scanning calorimeter (RDC220 manufactured by SEIKO Electronics Industries) in accordance with JIS K7121-1987 and JIS K7122-1987. A 5 mg polyester film was used in the sample, and the temperature of the vertex of the endothermic peak obtained from the DSC curve when the temperature was raised from 25 ° C. to 300 ° C. at 20 ° C./min was set as the melting point. In addition, when the film is laminated, each layer of the film can be cut out according to the thickness of the laminated layer, and the melting point of each element of the layer can be measured. Yu Benfa In the Ming Dynasty, in the case of a laminated polyester film having a polyester A layer and a polyester B layer, the melting point of each layer is measured, the layer with the higher melting point is referred to as the polyester A layer, and the lower layer is referred to as the polyester B. Floor.

(5)結晶熔解前之微小吸熱尖峰溫度(Tmeta) (5) Tiny endothermic peak temperature before crystal melting (Tmeta)

使用差示掃描熱量計(SEIKO電子工業製RDC220),依據JIS K7121-1987、JIS K7122-1987,進行測定及解析。於樣品中使用5mg聚酯薄膜,將自25℃起以20℃/分鐘升溫至300℃為止時的結晶熔解峰之前所出現的微小吸熱尖峰溫度讀取成Tmeta。 Measurement and analysis were performed using a differential scanning calorimeter (RDC220 manufactured by SEIKO Electronics Industries) in accordance with JIS K7121-1987 and JIS K7122-1987. A 5 mg polyester film was used in the sample, and the tiny endothermic peak temperature that appeared before the crystal melting peak when the temperature was raised from 25 ° C to 300 ° C at 20 ° C / min was read as Tmeta.

(6)1000mm寬度薄膜之主配向軸、配向角最大值 (6) The main alignment axis and the maximum value of the alignment angle of the 1000mm width film

於薄膜的任意點,以100mm×100mm之尺寸切出樣品,使用KS Systems製(現王子計測機器)之微波分子配向計MOA-2001A(頻率4GHz),求得聚酯薄膜之面內的主配向軸,當作TD方向。又,以此任意點作為薄膜的TD方向之中心,在TD方向的任意之一方向(A方向)的50mm~500mm間每50mm(50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm)之位置,及自薄膜的TD方向之中心起,在TD方向之與A方向相反的方向(B方向)之50mm~500mm間每50mm之位置,使用上述微波分子配向計MOA-2001A(頻率4GHz),測定配向角(主配向軸與薄膜TD方向或薄膜MD方向所成之角度中小者的角度),求得其最大值。 At any point of the film, cut out a sample with a size of 100 mm × 100 mm, and use the microwave molecular alignment meter MOA-2001A (frequency 4 GHz) manufactured by KS Systems (now Oji measuring equipment) to determine the main alignment in the plane of the polyester film. Axis as the TD direction. Also, using this arbitrary point as the center of the TD direction of the film, every 50mm (50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 50mm to 500mm) between 50mm and 500mm in any one of the TD directions (A direction). 450mm, 500mm), and from the center of the TD direction of the film, every 50mm between 50mm and 500mm in the TD direction opposite to the A direction (B direction), using the above-mentioned microwave molecular alignment meter MOA-2001A (Frequency 4 GHz), the alignment angle (the smaller of the angles formed by the main alignment axis and the film TD direction or the film MD direction) was measured, and the maximum value was obtained.

(7)藉由溫度調變DSC求得的玻璃轉移溫度 (7) Glass transition temperature determined by temperature-modulated DSC

與(6)同樣地,於薄膜任意之點,以100mm×100mm之尺寸切出樣品,由其中採取5mg,置入鋁製標準容器 內,使用差示掃描熱量計(TA Instrument製Q100),於氣流環境下(流速50mL/分鐘)在0℃至200℃之範圍,以2℃/分鐘、溫度調變週期為60秒且溫度調變振幅1℃的正弦波狀實施測定。再者,比熱校正係以藍寶石實施,於數據解析中使用TA Instrument公司製「Universal Analysis 2000」。於所得之可逆成分的溫度調變DSC圖之階梯狀的變化部分中,對於玻璃轉移溫度,藉由與JISK7121(1987)的「9.3玻璃轉移溫度之求得方式(1)中間點玻璃轉移溫度Tmg」記載之方法同樣之方法,求得溫度調變DSC之玻璃轉移溫度(將自各基線的延長直線起在縱軸方向等距離之直線與玻璃轉移的階梯狀變化部分之曲線所相交之點當作溫度調變DSC的玻璃轉移溫度)。又,以此任意之點作為薄膜的TD方向之中心,在TD方向的任意之一方向(A方向)的每50mm~500mm(50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm)之位置,及自薄膜的TD方向之中心起,在TD方向之與A方向相反的方向(B方向)的50mm~500mm間每50mm之位置,使用上述差示掃描熱量計,測定玻璃轉移溫度,求得其最低溫度。 As in (6), cut out a sample at any point of the film with a size of 100mm × 100mm, take 5mg from it, and place it in an aluminum standard container Within the range, a differential scanning calorimeter (Q100, manufactured by TA Instrument) was used in an airflow environment (flow rate: 50 mL / min) in the range of 0 ° C to 200 ° C, at a temperature of 2 ° C / min, with a temperature adjustment cycle of 60 seconds, and temperature adjustment. The measurement was performed in a sine wave shape with a variable amplitude of 1 ° C. The specific heat correction is performed using sapphire, and "Universal Analysis 2000" manufactured by TA Instrument was used for data analysis. In the step-like change portion of the temperature-modulated DSC chart of the obtained reversible component, the glass transition temperature was determined in accordance with JIS K7121 (1987), "9.3 Method for Determining Glass Transition Temperature. "The method described in the same way, to determine the glass transition temperature of the temperature-modulated DSC (take the intersection of a straight line at an equal distance in the vertical axis direction from the extended straight line of each baseline with the curve of the step-shaped change portion of the glass transition as Temperature-modulated DSC glass transition temperature). In addition, this point is used as the center of the TD direction of the film, and every 50mm to 500mm (50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 450mm) in any one of the TD directions (A direction). , 500mm), and from the center of the TD direction of the film, every 50mm between 50mm and 500mm in the TD direction opposite to the A direction (B direction), using the above differential scanning calorimeter to measure the glass Transfer the temperature to find its minimum temperature.

(8)在150℃的薄膜MD方向之10%伸張時應力 (8) Tensile stress at 10% of MD direction of film at 150 ° C

將薄膜在MD方向中切出長度150mm×寬度10mm之矩形,當作樣品。使用拉伸試驗機(ORIENTEC製Tensilon UCT-100),初期拉伸夾頭間距離為50mm,拉伸速度為300mm/分鐘,在薄膜的MD方向中進行拉伸試驗。測定係於經預先設定在150℃的恆溫槽中固定薄膜樣品,於90 秒的預熱後,進行拉伸試驗。讀取樣品伸張10%時(夾頭間距離成為55mm時)的施加於薄膜之荷重,將其除以試驗前的試料之截面積(薄膜厚度×10mm)所得之值設為10%伸張時應力。再者,測定係將薄膜的任意位置之主配向軸方向當作TD方向,以該位置作為中心(TD方向中心),沿著TD方向於2方向各自取550mm寬度,對於1100mm寬度之薄膜的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反的方向(B方向)的500mm之位置的3點,各自進行5次,將其15個值的平均值設為在150℃的薄膜MD方向10%伸張時應力。 A rectangle with a length of 150 mm and a width of 10 mm was cut out in the MD direction as a sample. A tensile tester (Tensilon UCT-100 manufactured by ORIENTEC) was used, and the initial tensile chuck distance was 50 mm and the tensile speed was 300 mm / min. The tensile test was performed in the MD direction of the film. The measurement is based on a film sample fixed in a constant temperature bath set at 150 ° C at 90 ° C. After a second warm-up, a tensile test was performed. The load applied to the film when the sample was stretched at 10% (when the distance between the chucks was 55mm) was divided by the cross-sectional area of the sample before the test (thickness of the film × 10mm). The stress was set at 10%. . In addition, the measurement is based on the main alignment axis direction of the arbitrary position of the film as the TD direction, with the position as the center (the center of the TD direction), and a width of 550 mm in each of two directions along the TD direction. The center of the direction, the position of 500 mm in any one of the TD directions (A direction) from the center, and the position of 500 mm in the TD direction opposite to the A direction (B direction) from the center are each performed 5 points Next, the average value of 15 values was set as the stress at the time of 10% stretching in the MD direction of the film at 150 ° C.

(9)熱收縮率(150℃、190℃) (9) Thermal shrinkage (150 ° C, 190 ° C)

將薄膜在MD方向及TD方向中各自切出長度150mm×寬度10mm的矩形,當作樣品。於樣品上以100mm之間隔(自中央部起往兩端50mm之位置)描繪標線,吊掛3g的秤錘,於經加熱到指定溫度(150℃、190℃)的熱風烘箱內放置30分鐘,進行加熱處理。測定熱處理後的標線間距離,自加熱前後的標線間距離之變化,藉由下述式算出熱收縮率。再者,評價係將薄膜的任意位置之主配向軸方向當作TD方向,以該位置作為中心(TD方向中心),沿著TD方向採集2方向各自550mm寬度,對於1100mm寬度的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反的方向(B方向)的500mm之位置的3點各自進行5次,將其15個值的平均值設為在指定溫度(150℃、190℃)的薄膜 MD方向及TD方向之熱收縮率。 A rectangle having a length of 150 mm and a width of 10 mm was cut out of the film in the MD direction and the TD direction, respectively, and used as samples. Draw a marking line on the sample at 100mm intervals (50mm from the center to both ends), hang a 3g scale weight, and place in a hot air oven heated to the specified temperature (150 ° C, 190 ° C) for 30 minutes For heat treatment. The distance between the graticules after the heat treatment was measured, and the change in the distance between the graticules before and after heating was measured, and the thermal shrinkage was calculated by the following formula. In addition, the evaluation is based on the main alignment axis direction at any position of the film as the TD direction, with the position as the center (the center of the TD direction), and the width of 550 mm in each of the two directions is collected along the TD direction. The three positions of 500 mm in any one of the TD directions (A direction) from the center and 500 mm in the TD direction opposite to the A direction (B direction) from the center are performed 5 times each, and An average of 15 values is set to a film at a specified temperature (150 ° C, 190 ° C) Thermal shrinkage in MD and TD directions.

熱收縮率(%)={(加熱處理前的標線間距離)-(加熱處理後的標線間距離)}/(加熱處理前的標線間距離)×100。 Thermal shrinkage (%) = {(distance between graticules before heat treatment)-(distance between graticules after heat treatment)} / (distance between graticules before heat treatment) × 100.

(10)式(I)、式(II)算出方法 (10) Calculation method of formula (I) and formula (II)

與(9)同樣地,進行1100mm寬度薄膜的TD方向之中心值的MD、TD方向之190℃的熱收縮率(SCMD、SCTD)、自1100mm寬度薄膜的寬度方向之中心起,在TD方向的任意之一方向(A方向)的500mm之位置的MD、TD方向之190℃的熱收縮率(SAMD、SATD)、自1100mm寬度薄膜的TD方向之中心起,在TD方向之與A方向相反的方向(B方向)的500mm之位置的MD、TD方向之190℃的熱收縮率(SBMD、SBTD)之測定(採用各自5次測定之平均值),進行式(I)、式(II)的左邊之值的算出。 As in (9), the MD of the center value of the 1100 mm-thick film in the TD direction and the thermal shrinkage rate (SC MD , SC TD ) of 190 ° C in the TD direction are performed from the center of the width direction of the 1100 mm-thick film in the TD direction. MD at 500mm in either direction (A direction), thermal shrinkage (SA MD , SA TD ) of 190 ° C at TD direction, from the center of the TD direction of the 1100mm-thick film in the TD direction The heat shrinkage (SB MD , SB TD ) of the MD at 500 mm in the opposite direction (B direction) and 190 ° C in the TD direction was measured (using the average of 5 measurements each), and formula (I) was performed. Calculate the value on the left side of formula (II).

(SAMD+SBMD)/SCMD×2≦1.2 (I) (SA MD + SB MD ) / SC MD × 2 ≦ 1.2 (I)

(SATD+SBTD)/SCTD×2≦1.2 (II)。 (SA TD + SB TD ) / SC TD × 2 ≦ 1.2 (II).

(11)面配向係數 (11) Surface alignment coefficient

以鈉D線(波長589nm)作為光源,使用阿貝折射計,測定薄膜的MD方向之折射率(nMD)、TD方向之折射率(nTD)、厚度方向之折射率(nZD),自下述式算出面配向係數(fn)。 Using the sodium D-line (wavelength 589nm) as the light source, using an Abbe refractometer to measure the refractive index in the MD direction (n MD ), the refractive index in the TD direction (n TD ), and the refractive index in the thickness direction (n ZD ), The surface alignment coefficient (fn) was calculated from the following formula.

fn=(nMD+nTD)/2-nZD fn = (n MD + n TD ) / 2-n ZD

面配向係數係對於薄膜的兩面進行測定,表中記載高者的面配向係數之值。 The surface alignment coefficient is measured on both sides of the film, and the value of the higher surface alignment coefficient is described in the table.

再者,測定係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(TD方向中心),沿 著TD方向採集2方向各自550mm寬度,對於1100mm寬度之薄膜的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反的方向(B方向)的500mm之位置的3點,各自進行5次,採用其15個值之平均值。 In addition, the measurement is performed by setting the main alignment axis direction of an arbitrary position of the film to the TD direction, and using the position as the center (the center of the TD direction) along the Collect 550mm widths in two directions in the TD direction. For the center of the TD direction of a film with a width of 1100mm, the position of 500mm in any one direction (A direction) from the center, and the TD direction from the center is opposite to the A direction. Three points at a position of 500 mm in the direction (direction B) were performed 5 times each, and an average of 15 values was used.

(12)熱機械分析(TMA) (12) Thermomechanical analysis (TMA)

將薄膜在MD方向及TD方向中切出長度50mm×寬度4mm之矩形,當作樣品,使用熱機械分析裝置(SEIKO儀器製TMAEXSTAR6000),於下述條件下升溫,算出在25℃至200℃的伸張尖峰溫度。 A rectangle with a length of 50 mm and a width of 4 mm was cut out of the film in the MD direction and the TD direction. As a sample, a thermomechanical analysis device (TMAEXSTAR 6000 manufactured by SEIKO Instruments) was used, and the temperature was raised under the following conditions to calculate the temperature at 25 to 200 Stretch peak temperature.

試樣長度:15mm,荷重:19.6mN,升溫速度:5℃/分鐘,測定溫度範圍:25~200℃ Sample length: 15mm, load: 19.6mN, heating rate: 5 ° C / min, measurement temperature range: 25 ~ 200 ° C

本發明中在25℃至200℃的伸張尖峰溫度,係指隨著升溫進行伸張之薄膜轉移至收縮行為之溫度。薄膜一旦收縮後,亦可再度轉移至伸張行為之情況,但於本發明中,將自25℃至200℃為止升溫時的最初由伸張行為轉移至收縮行為的溫度設為薄膜MD方向、TD方向的伸張尖峰溫度。 In the present invention, the stretching peak temperature at 25 ° C to 200 ° C refers to the temperature at which the stretched film is stretched to shrinkage behavior with increasing temperature. Once the film has shrunk, it can transition to the stretching behavior again. However, in the present invention, the temperature at which the transition from the stretching behavior to the shrinking behavior is initially set as the MD direction and TD direction of the film when the temperature rises from 25 ° C to 200 ° C. Spike temperature.

再者,測定係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心(TD方向中心),沿著TD方向採集2方向各自550mm寬度,對於1100mm寬度之薄膜的TD方向之中心、自中心起TD方向的任意之一方向(A方向)的500mm之位置、自中心起TD方向之與A方向相反的方向(B方向)的500mm之位置的3點,MD、TD皆各自進行3次,採用對於MD、TD所測定的9個值之平均值。 In addition, the measurement is performed by setting the main alignment axis direction of the arbitrary position of the film to the TD direction, and using this position as the center (TD direction center), collecting the width of 550 mm in each of the two directions along the TD direction, and the TD direction of the film having a width of 1100 mm 3 points of the center, 500mm position in any one of the TD directions (A direction) from the center, and 500mm position in the TD direction opposite to the A direction (B direction) from the center, both MD and TD are Each measurement was performed 3 times, and the average value of 9 values measured for MD and TD was used.

(13)尺寸安定性 (13) Dimensional stability

於1100mm寬度的聚酯薄膜表面上,用模塗布機將聚芳酯/MEK分散體進行塗布、乾燥(乾燥溫度:150℃,乾燥時間:1分鐘,捲出張力:200N/m,捲繞張力:100N/m)。測定乾燥後的聚酯薄膜之寬度,以下述基準進行評價(乾燥後的聚芳酯厚度為25μm)。 On the surface of a polyester film with a width of 1100 mm, the polyarylate / MEK dispersion was coated and dried with a die coater (drying temperature: 150 ° C, drying time: 1 minute, unwinding tension: 200 N / m, winding tension : 100 N / m). The width of the polyester film after drying was measured and evaluated according to the following criteria (thickness of the polyarylate after drying was 25 μm).

A:寬度縮幅小於5mm(乾燥後的聚酯薄膜之寬度為995mm以上)。 A: The width shrinkage is less than 5 mm (the width of the polyester film after drying is 995 mm or more).

B:寬度縮幅為5mm以上且小於10mm(乾燥後的聚酯薄膜之寬度為990mm以上且小於995mm)。 B: The width shrinkage is 5 mm or more and less than 10 mm (the width of the polyester film after drying is 990 mm or more and less than 995 mm).

C:寬度縮幅為10mm以上(乾燥後的聚酯薄膜之寬度小於990mm)。 C: The width shrinkage is 10 mm or more (the width of the polyester film after drying is less than 990 mm).

再者,寬度縮幅的評價係選定塗布‧乾燥後 的1000mm寬度薄膜之任意10處,進行寬度測定,採用其(1000mm寬度-任意10處的薄膜寬度平均值)作為寬度縮幅量。 In addition, the evaluation of width reduction is selected after coating and drying Measure the width at any 10 places of the 1000mm width film, and use it (1000mm width-the average value of the film width at any 10 places) as the width shrinkage.

(14)成型加工性 (14) Moldability

將(13)所得之經聚芳酯塗布的聚酯薄膜投入熱風烘箱內,在長度方向中進行單軸延伸(烘箱溫度:150℃,寬度方向自由)。對於薄膜的延伸性(成型加工性),以下述基準進行評價。 The polyarylate-coated polyester film obtained in (13) was put into a hot air oven and uniaxially stretched in the longitudinal direction (oven temperature: 150 ° C, width direction free). The stretchability (moldability) of the film was evaluated based on the following criteria.

A:以延伸張力小於1200N/m,可1.1倍延伸。 A: With an extension tension of less than 1200 N / m, it can be extended 1.1 times.

B:以延伸張力1200N/m以上且小於1500N/m,可1.1倍延伸。 B: It can be extended 1.1 times with an extension tension of 1200 N / m or more and less than 1500 N / m.

C:以延伸張力1500N/m,無法1.1倍延伸。 C: It cannot be extended by 1.1 times with an extension tension of 1500 N / m.

(15)機能性塗膜寬度方向均勻性 (15) Functional uniformity in width direction

自(14)所得之聚芳酯塗布單軸延伸聚酯薄膜剝離聚芳酯層,對於寬度方向之中心、自中心起寬度方向的任意之一方向(A方向)的500mm之位置、自中心起寬度方向之與A方向相反的方向(B方向)的500mm之位置的3點測定面內遲滯值,並以下述基準進行評價。再者,遲滯值係使用(新王子計測機器製自動雙折射計(KOBRA-21ADH)進行測定。 From the polyarylate coated uniaxially stretched polyester film obtained in (14), the polyarylate layer is peeled off, and from the center of the width direction, at a position of 500 mm in any direction (A direction) from the center, from the center The in-plane hysteresis value was measured at three points at a position of 500 mm in a direction opposite to the A direction (B direction) in the width direction, and evaluated based on the following criteria. In addition, the hysteresis value was measured using the automatic birefringence meter (KOBRA-21ADH made by Shin-Oji Measurement Instruments).

A:3點測定的遲滯值之最大值與最小值之差小於10nm。 A: The difference between the maximum value and the minimum value of the hysteresis value measured at three points is less than 10 nm.

B:3點測定的遲滯值之最大值與最小值之差為10nm以上且小於20nm。 B: The difference between the maximum value and the minimum value of the hysteresis value measured at three points is 10 nm or more and less than 20 nm.

C:3點測定的遲滯值之最大值與最小值之差為20nm以上。 C: The difference between the maximum value and the minimum value of the hysteresis value measured at three points is 20 nm or more.

(聚酯之製造) (Production of polyester)

供製膜的聚酯樹脂係如以下地準備。 The polyester resin for film formation is prepared as follows.

(聚酯A) (Polyester A)

作為二羧酸成分的對苯二甲酸成分為100莫耳%、作為二醇成分的乙二醇成分為100莫耳%之聚對苯二甲酸乙二酯樹脂(固有黏度0.65)。 A polyethylene terephthalate resin (inherent viscosity 0.65) having a terephthalic acid component as a dicarboxylic acid component of 100 mole% and a glycol component as a glycol component of 100 mole%.

(聚酯B) (Polyester B)

將1,4-環己烷二甲醇相對於二醇成分共聚合33mol%而成之共聚合聚酯(EASTMAN化學公司製GN001),作為環己烷二甲醇共聚合聚對苯二甲酸乙二酯使用(固有黏度0.75)。 Copolymerized polyester (GN001, manufactured by Eastman Chemical Co., Ltd.) by copolymerizing 1,4-cyclohexanedimethanol with 33 mol% of the diol component, and copolymerized polyethylene terephthalate as cyclohexanedimethanol. Used (inherent viscosity 0.75).

(聚酯C) (Polyester C)

作為二羧酸成分的對苯二甲酸成分為100莫耳%、作為二醇成分的乙二醇成分為70莫耳%、新戊二醇成分為30莫耳%之新戊二醇共聚合聚對苯二甲酸乙二酯樹脂(固有黏度0.75)。 Copolymerization of neopentyl glycol with a terephthalic acid component as a dicarboxylic acid component of 100 mol%, a glycol component as a diol component of 70 mol%, and a neopentyl glycol component of 30 mol% Ethylene terephthalate resin (inherent viscosity 0.75).

(聚酯D) (Polyester D)

作為二羧酸成分的對苯二甲酸成分為100莫耳%、作為二醇成分的乙二醇成分為85莫耳%、二乙二醇成分為15莫耳%之二乙二醇共聚合聚對苯二甲酸乙二酯樹脂(固有黏度0.65)。 Diethylene glycol copolymerized with 100% by mole of terephthalic acid as dicarboxylic acid component, 85% by mole of ethylene glycol as diol component, and 15% by mole of diethylene glycol. Ethylene terephthalate resin (inherent viscosity 0.65).

(聚酯E) (Polyester E)

作為二羧酸成分的對苯二甲酸成分為82.5莫耳%、間苯二甲酸成分為17.5莫耳%、作為二醇成分的乙二醇成分為100莫耳%之間苯二甲酸共聚合聚對苯二甲酸乙二酯樹脂(固有黏度0.7)。 The terephthalic acid component as the dicarboxylic acid component is 82.5 mole%, the isophthalic acid component is 17.5 mole%, and the ethylene glycol component as the diol component is 100 mole%. Ethylene terephthalate resin (inherent viscosity 0.7).

(聚酯F) (Polyester F)

作為二羧酸成分的對苯二甲酸成分為85莫耳%、2,6-萘二羧酸成分為15莫耳%、作為二醇成分的乙二醇成分為100莫耳%之2,6-萘二羧酸共聚合聚對苯二甲酸乙二酯樹脂(固有黏度0.7)。 The terephthalic acid component as the dicarboxylic acid component is 85 mol%, the 2,6-naphthalenedicarboxylic acid component is 15 mol%, and the ethylene glycol component as the diol component is 2,6 of 100 mol%. -Naphthalenedicarboxylic acid copolymerized polyethylene terephthalate resin (inherent viscosity 0.7).

(粒子母料) (Particle Masterbatch)

於聚酯A中以2質量%的粒子濃度含有數平均粒徑2.2μm的凝聚矽石粒子而成之聚對苯二甲酸乙二酯粒子母料(固有黏度0.65)。 A polyethylene terephthalate particle masterbatch (intrinsic viscosity 0.65) made of agglomerated silica particles having a number average particle diameter of 2.2 μm in a polyester concentration of 2% by mass.

(實施例1) (Example 1)

組成係如表中,將原料供給至各自氧濃度設為0.2體積%的各個排氣同方向雙軸擠壓機,並在A層擠壓機料筒溫度為270℃,B層擠壓機料筒溫度為277℃的情況下進行熔融,A層與B層合流後的短管溫度為277℃,噴嘴溫度為280℃,藉由T模頭在經溫度控制在25℃的冷卻滾筒上吐出片狀。於該情況下,使用直徑0.1mm的線狀電極來施加靜電,而使緊貼於冷卻滾筒,得到未延伸片。其次,於對長度方向的延伸前,在加熱輥上使薄膜溫度上升,以延伸溫度85℃,在長度方向中延伸3.1倍,立刻以經溫度控制在40℃的金屬輥來冷卻化。 The composition system is as shown in the table. The raw materials are supplied to each exhaust biaxial extruder in the same direction with an oxygen concentration of 0.2% by volume, and the barrel temperature of the layer A extruder is 270 ° C. The barrel temperature is 277 ° C. The short tube temperature after layer A and B are merged is 277 ° C, and the nozzle temperature is 280 ° C. The sheet is ejected by a T die on a cooling roller controlled by temperature at 25 ° C. shape. In this case, static electricity was applied using a linear electrode with a diameter of 0.1 mm, and it was brought into close contact with a cooling drum to obtain an unstretched sheet. Secondly, before stretching in the longitudinal direction, the film temperature was raised on a heating roller, the stretching temperature was 85 ° C, and the film was stretched 3.1 times in the longitudinal direction, and immediately cooled by a metal roller whose temperature was controlled at 40 ° C.

其次,以拉幅機式橫延伸機,在95℃的延伸前半溫度、105℃的延伸中途溫度、140℃的延伸後半溫度,於寬度方向中延伸3.9倍,直接在拉幅機內,以200℃的熱處理前半溫度、230℃的熱處理中途溫度進行熱處理,以180℃的熱處理後半溫度,邊在寬度方向中施予3%的鬆弛邊進行熱處理,得到薄膜厚度75μm之雙軸配向聚酯薄膜。 Secondly, the tenter type horizontal stretcher stretches 3.9 times in the width direction at the first half temperature of 95 ° C, the middle temperature of 105 ° C, and the second half temperature of 140 ° C. It is directly in the tenter at 200 °. The heat treatment was performed at a temperature of half before the heat treatment at 230 ° C and a temperature halfway through the heat treatment at 230 ° C. The heat treatment was performed at a temperature half after the heat treatment at 180 ° C while applying 3% relaxation in the width direction to obtain a biaxially oriented polyester film having a film thickness of 75 μm.

(實施例2) (Example 2)

除了如表中變更組成以外,與實施例1同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was changed as shown in the table.

(實施例3) (Example 3)

除了如表中變更組成以外,與實施例1同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was changed as shown in the table.

(實施例4) (Example 4)

除了於熱處理前半,在寬度方向中進行5%微延伸以 外,與實施例3同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 Except for the first half of the heat treatment, 5% micro-elongation in the width direction to A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 3.

(實施例5) (Example 5)

除了如表中變更組成以外,與實施例1同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was changed as shown in the table.

(實施例6) (Example 6)

除了如表中變更組成以外,與實施例1同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was changed as shown in the table.

(實施例7) (Example 7)

成為A/B/A之3層積層薄膜。各層的組成係如表中,將A層用之原料與B層用之原料供給至各自氧濃度設為0.2體積%的各個排氣同方向雙軸擠壓機,並在A層擠壓機料筒溫度為270℃,B層擠壓機料筒溫度為277℃的情況下進行熔融,A層與B層合流後的短管溫度為277℃,噴嘴溫度為280℃,藉由T模頭在經溫度控制在25℃的冷卻滾筒上吐出片狀。於該情況下,使用直徑0.1mm的線狀電極來施加靜電,而使緊貼於冷卻滾筒,得到包含A層/B層/A層之3層積層未延伸薄膜。 A three-layer laminated film of A / B / A. The composition of each layer is as shown in the table. The raw material for layer A and the raw material for layer B are supplied to each exhaust co-axial biaxial extruder with an oxygen concentration of 0.2% by volume, and the material is extruded in layer A. The barrel temperature is 270 ° C. The melting of the extruder barrel temperature is 277 ° C. The short tube temperature after layer A and B merge is 277 ° C and the nozzle temperature is 280 ° C. The sheet was discharged on a cooling drum controlled by temperature at 25 ° C. In this case, a static electrode was applied using a linear electrode having a diameter of 0.1 mm, and it was brought into close contact with a cooling drum to obtain a three-layer laminated unstretched film including A layer / B layer / A layer.

然後,除了使熱處理中途溫度成為225℃以外,與實施例1同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 Then, a biaxially-oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the temperature during the heat treatment was 225 ° C.

(實施例8) (Example 8)

除了如表中變更組成,於熱處理前半,在寬度方向中進行2%微延伸以外,與實施例7同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 7 except that the composition was changed as shown in the table, and 2% of micro-elongation was performed in the width direction in the first half of the heat treatment.

(實施例9) (Example 9)

除了如表中變更組成,於熱處理前半,在寬度方向中進行5%微延伸以外,與實施例7同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially-oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 7 except that the composition was changed as shown in the table, and 5% micro-elongation was performed in the width direction in the first half of the heat treatment.

(實施例10) (Example 10)

除了如表中變更組成,於熱處理前半,在寬度方向中進行5%微延伸,更且於熱處理中途,在寬度方向中進行3%微延伸以外,與實施例7同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 Except changing the composition as shown in the table, in the first half of the heat treatment, 5% micro-elongation was performed in the width direction, and during the heat treatment, 3% micro-elongation was performed in the width direction. In the same manner as in Example 7, a film thickness of 75 μm was obtained. Shaft alignment polyester film.

(實施例11) (Example 11)

除了如表中變更組成,使熱處理中途溫度成為205℃以外,與實施例7同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 7 except that the composition was changed as shown in the table and the temperature during the heat treatment was 205 ° C.

(實施例12) (Example 12)

除了如表中變更組成,使熱處理中途溫度成為230℃以外,與實施例7同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 7 except that the composition was changed as shown in the table and the temperature during the heat treatment was changed to 230 ° C.

(實施例13) (Example 13)

除了如表中變更組成,於熱處理前半,在寬度方向中進行5%微延伸,更且於熱處理中途,在寬度方向中進行3%微延伸以外,與實施例7同樣地得到薄膜厚度50μm之雙軸配向聚酯薄膜。 Except for changing the composition as shown in the table, in the first half of the heat treatment, 5% micro-elongation was performed in the width direction, and in the middle of the heat treatment, 3% micro-elongation was performed in the width direction. In the same manner as in Example 7, a film thickness of 50 μm was obtained. Shaft alignment polyester film.

(實施例14) (Example 14)

除了如表中變更組成,於熱處理前半,在寬度方向中進行5%微延伸,更且熱處理中途,在寬度方向中進行3%微延伸以外,與實施例7同樣地得到薄膜厚度75μm之 雙軸配向聚酯薄膜。 A film thickness of 75 μm was obtained in the same manner as in Example 7 except that the composition was changed as shown in the table, 5% micro-elongation was performed in the width direction in the first half of the heat treatment, and 3% micro-elongation was performed in the width direction during the heat treatment. Biaxially oriented polyester film.

(實施例15) (Example 15)

於實施例14所得之雙軸配向聚酯薄膜,一邊在180℃的熱風烘箱中使寬度方向自由,使長度方向的捲繞速度比捲出速度低1%,一邊進行離線退火處理。 The biaxially oriented polyester film obtained in Example 14 was subjected to off-line annealing while leaving the width direction free in a hot air oven at 180 ° C. and making the winding speed in the longitudinal direction lower than the unwinding speed by 1%.

(實施例16) (Example 16)

除了如表中變更組成,熱處理中途溫度為235℃,進行熱處理以外,與實施例1同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film with a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was changed as shown in the table, and the temperature was 235 ° C. during the heat treatment.

(實施例17) (Example 17)

除了如表中變更組成,與實施例10同樣地得到薄膜厚度75μm之雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 10 except that the composition was changed as shown in the table.

(比較例1) (Comparative example 1)

除了如表中變更組成,橫延伸前半、中途、後半溫度皆為120℃,延伸3.4倍,直接在拉幅機內,以熱處理前半溫度、熱處理中途溫度230℃進行熱處理,以熱處理後半溫度180℃,邊在寬度方向施予3%的鬆弛邊進行熱處理以外,與實施例7同樣地得到薄膜厚度75μm的雙軸配向聚酯薄膜。 Except for changing the composition as shown in the table, the temperature of the first half, halfway, and second half of the horizontal stretching is 120 ° C, which is 3.4 times longer. Directly in the tenter, heat treatment is performed at the first half of the heat treatment and the midway temperature of 230 ° C, and the second half of the heat treatment is 180 ° C. A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 7 except that heat treatment was performed while applying 3% relaxation in the width direction.

(比較例2) (Comparative example 2)

除了組成如表中,熱處理中途溫度為220℃以外,與實施例1同樣地得到薄膜厚度75μm的雙軸配向聚酯薄膜。 A biaxially oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was as shown in the table and the temperature during the heat treatment was 220 ° C.

(比較例3) (Comparative example 3)

除了組成如表中,熱處理中途溫度為195℃,與實施例1同樣地得到薄膜厚度75μm的雙軸配向聚酯薄膜。 A biaxially-oriented polyester film having a film thickness of 75 μm was obtained in the same manner as in Example 1 except that the composition was as shown in the table and the temperature during the heat treatment was 195 ° C.

表中的縮寫符號之意思係如以下。 The meanings of the abbreviations in the table are as follows.

EG:乙二醇 EG: ethylene glycol

CHDM:1,4-環己烷二甲醇 CHDM: 1,4-cyclohexanedimethanol

DEG:二乙二醇 DEG: Diethylene glycol

NPG:新戊二醇 NPG: neopentyl glycol

TPA:對苯二甲酸 TPA: terephthalic acid

IPA:間苯二甲酸 IPA: isophthalic acid

NDC:2,6-萘二羧酸 NDC: 2,6-naphthalenedicarboxylic acid

[產業上之可利用性] [Industrial availability]

本發明之雙軸配向聚酯薄膜,係由於在150℃的成型應力低而易成型性良好,且由於150℃之熱收縮率低而塗布乾燥時的薄膜變形小,更且由於1000mm寬度的薄膜之配向角的最大值小而寬度方向的物性均勻性優異,可適用於建材、行動機器、電機製品、汽車零件、遊戲機零件等之成型裝飾用途、偏光板等之光學用薄膜等。 The biaxially oriented polyester film of the present invention has good moldability due to low forming stress at 150 ° C, and small deformation of the film during coating and drying due to low thermal shrinkage at 150 ° C, and moreover, due to a film having a width of 1000 mm The maximum value of the alignment angle is small and the physical property uniformity in the width direction is excellent. It can be applied to the molding and decoration of building materials, mobile equipment, motor products, automobile parts, game machine parts, and optical films such as polarizing plates.

Claims (12)

一種雙軸配向聚酯薄膜,其在150℃的薄膜MD(machine direction,縱向)方向之10%伸張時應力為5MPa以上30MPa以下,在150℃的薄膜MD方向之熱收縮率為5%以下,且1000mm寬度中的薄膜之配向角(主配向軸與薄膜TD(transverse direction,橫向)方向或薄膜MD方向所成之角度中小者的角度)之最大值為20°以下;其中,1000mm寬度的薄膜之配向角,係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心,沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜,於自該任意之點起往TD方向兩端在50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm之位置(1000mm寬度),測定配向角,求得其中之最大值;而且,於同一薄膜面內將與TD方向呈正交的方向設為MD方向。A biaxially oriented polyester film having a tensile stress of 5 MPa or more and 30 MPa or less at 10% of the MD (machine direction) direction of the film at 150 ° C, and a thermal shrinkage of 5% or less at the MD direction of the film at 150 ° C. And the maximum value of the alignment angle of the film in the 1000 mm width (the angle between the main alignment axis and the film TD (transverse direction) direction or the angle formed by the film MD direction) is less than 20 °; The alignment angle is to set the main alignment axis direction of the arbitrary position of the film to the TD direction, with this position as the center, and take a width of 550mm in 2 directions along the TD direction to make a film with a width of 1100mm. Point the two ends in the TD direction at 50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 450mm, and 500mm (1000mm width), and measure the alignment angle to find the maximum value. The direction orthogonal to the TD direction in the plane is referred to as the MD direction. 如請求項1之雙軸配向聚酯薄膜,其係MD方向10m以上、TD方向1100mm以上之薄膜。For example, the biaxially oriented polyester film of claim 1, which is a film of 10 m or more in the MD direction and 1100 mm or more in the TD direction. 如請求項1或2之雙軸配向聚酯薄膜,其中1000mm寬度中的薄膜之藉由溫度調變DSC所求得之玻璃轉移溫度的最低溫度為80℃以上110℃以下;其中,1000mm寬度中的薄膜之藉由溫度調變DSC所求得之玻璃轉移溫度,係將薄膜的任意位置之主配向軸方向設為TD方向,以該位置作為中心,沿著TD方向於2方向各自取550mm寬度,作成寬度為1100mm之薄膜,於自該任意之點起往TD方向兩端在50mm、100mm、150mm、200mm、250mm、300mm、350mm、400mm、450mm、500mm位置(1000mm寬度),測定玻璃轉移溫度,求得其中之最低溫度。For example, if the biaxially oriented polyester film of claim 1 or 2 is used, the minimum temperature of the glass transition temperature of the film in 1000mm width determined by temperature modulation DSC is 80 ° C or higher and 110 ° C or lower; The glass transition temperature of the thin film obtained by temperature-modulated DSC is set to the main alignment axis direction of any position of the film as the TD direction, with this position as the center, and a width of 550 mm in each of the two directions along the TD direction , Make a film with a width of 1100mm, and from the point to the end of the TD direction at 50mm, 100mm, 150mm, 200mm, 250mm, 300mm, 350mm, 400mm, 450mm, 500mm (1000mm width), and measure the glass transition temperature , Find the lowest temperature among them. 如請求項1或2之雙軸配向聚酯薄膜,其在190℃的薄膜MD方向與TD方向之熱收縮率為5%以下。For example, the biaxially oriented polyester film of claim 1 or 2 has a thermal shrinkage ratio of the film in the MD direction and the TD direction at 190 ° C of 5% or less. 如請求項1或2之雙軸配向聚酯薄膜,其滿足下述(I)式,(SAMD+SBMD)/(SCMD×2)≦1.2 (I)其中,SAMD:自1100mm寬度薄膜的TD方向之中心起,在TD方向的任意之一方向(A方向)的500mm之位置的MD方向之190℃熱收縮率;SBMD:自1100mm寬度薄膜的TD方向之中心起,在TD方向之與A方向相反的方向(B方向)的500mm之位置的MD方向之190℃熱收縮率;SCMD:在1100mm寬度薄膜的TD方向之中心的MD方向之190℃熱收縮率。For example, the biaxially oriented polyester film of claim 1 or 2 satisfies the following formula (I), (SA MD + SB MD ) / (SC MD × 2) ≦ 1.2 (I), where SA MD is from 1100mm width Thermal shrinkage at 190 ° C from the center of the TD direction of the film in the MD direction at a position of 500mm in any one of the TD directions (A direction); SB MD : from the center of the TD direction of the 1100mm film in TD Thermal shrinkage at 190 ° C in the MD direction at a position of 500 mm opposite to the direction A (B direction); SC MD : Thermal shrinkage at 190 ° C in the MD direction at the center of the TD direction of a 1100 mm-thick film. 如請求項1或2之雙軸配向聚酯薄膜,其滿足下述(II)式,(SATD+SBTD)/(SCTD×2)≦1.2 (II)其中,SATD:自1100mm寬度薄膜的TD方向之中心起,在TD方向的任意之一方向(A方向)的500mm之位置的TD方向之190℃熱收縮率;SBTD:自1100mm寬度薄膜的TD方向之中心起,在TD方向之與A方向相反的方向(B方向)的500mm之位置的TD方向之190℃熱收縮率;SCTD:在1100mm寬度薄膜的TD方向之中心的TD方向之190℃熱收縮率。If the biaxially oriented polyester film of claim 1 or 2 satisfies the following formula (II), (SA TD + SB TD ) / (SC TD × 2) ≦ 1.2 (II) Among them, SA TD : from 1100mm width Thermal shrinkage of 190 ° C in the TD direction from the center of the TD direction of the film at a position of 500mm in any one of the TD directions (A direction); SB TD : Starting from the center of the TD direction of a 1100mm-thick film, at the TD The thermal shrinkage rate of 190 ° C in the TD direction at a position of 500 mm opposite to the A direction (B direction); SC TD : the thermal shrinkage rate of 190 ° C in the TD direction at the center of the TD direction of a 1100 mm-thick film. 如請求項1或2之雙軸配向聚酯薄膜,其中在薄膜兩面的面配向係數之中,高者之面的面配向係數為0.111以上0.17以下。For example, the biaxially oriented polyester film of claim 1 or 2, wherein among the surface alignment coefficients of the two surfaces of the film, the surface alignment coefficient of the higher surface is 0.111 or more and 0.17 or less. 如請求項1或2之雙軸配向聚酯薄膜,其係具有聚酯A層與熔點比聚酯A層低的聚酯B層之積層聚酯薄膜,聚酯A層係位於至少一側之最外層。If the biaxially oriented polyester film of claim 1 or 2 is a laminated polyester film having a polyester A layer and a polyester B layer having a lower melting point than the polyester A layer, the polyester A layer is located on at least one side Outermost. 如請求項1或2之雙軸配向聚酯薄膜,其中於熱機械分析(TMA)中,以19.6mN的荷重,自25℃至200℃為止以5℃/分鐘的升溫速度升溫時之薄膜TD方向的伸張尖峰溫度為70℃以上。If the biaxially oriented polyester film of claim 1 or 2 is used, the film is TD when the temperature is raised in a thermomechanical analysis (TMA) with a load of 19.6mN from 25 ° C to 200 ° C at a temperature rise rate of 5 ° C / min. The stretching peak temperature in the direction is 70 ° C or higher. 如請求項1或2之雙軸配向聚酯薄膜,其中於熱機械分析(TMA)中,以19.6mN的荷重,自25℃至200℃為止以5℃/分鐘的升溫速度升溫時之薄膜MD方向的伸張尖峰溫度為60℃以上。If the biaxially oriented polyester film of claim 1 or 2 is used, the film MD when heated at a temperature of 5 ° C / min from 25 ° C to 200 ° C at a load of 19.6mN in thermomechanical analysis (TMA) The stretching peak temperature in the direction is 60 ° C or higher. 如請求項1或2之雙軸配向聚酯薄膜,其係使用於成型加工用途。If the biaxially oriented polyester film of claim 1 or 2 is used for molding processing. 如請求項1或2之雙軸配向聚酯薄膜,其係使用於光學用途。If the biaxially oriented polyester film of claim 1 or 2 is used for optical applications.
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