Biaxially stretched polyester film and process for producing the same

Abstract: A biaxially stretched polyester film being substantially free from scratches on the surface thereof and having a low heat shrinkage, a uniform thickness and an improved flatness is provided. The film according to the present invention is particularly useful as films for touch panels, membrane switches, etc. A process for producing the film also is provided.

Description: The present invention relates to a process for producing a biaxially stretched polyester film having an excellent thickness uniformity, low shrinkage characteristics and good flatness and also minimized in or substantially free of scratches or scuffs, from a substantially amorphous film principally composed of polyethylene terephthalate. For producing polyester films having a thickness of 25 µm or greater, a method has been known in which an amorphous sheet is stretched in the machine direction in a single step by using an IR heater. The polyester films obtained from such a method, however, were susceptible to scratches or scuffs in the course of their production process and also poor in thickness uniformity, flatness and shrinkage characteristics in comparison with thin polyester films. There has therefore been desired a process capable of producing a polyester film which can satisfy all of these property requirements. EP-B-0 022 278 discloses a process for producing a biaxially stretched polyester film wherein the stretching in the machine direction is conducted in a single step. EP-A-0 049 108 relates to a process for producing biaxially oriented polyester films wherein the film is first drawn in the longitudinal direction to an extent such that the resulting polyester film possesses a birefringence of from 0.001 to 0.012. The present inventors have pursued strenuous studies on the process for producing polyester films and, as a result, found that a polyester film which is hard to scratch and uniform in thickness can be obtained by employing a process which meets certain specific conditions. The present invention was achieved on the basis of such finding. It has been the problem underlying the present invention to provide a process for producing a biaxially stretched polyester film having an excellent thickness uniformity, low shrinkage characteristics and good flatness and being substantially free from scratches on the surface thereof. According to the present invention, this problem is solved by a process for producing a biaxially stretched polyester film according to claim 1. In accordance with the process of the present invention, there is provided a biaxially stretched polyester film of 25 to 500 µm thickness comprising, as the constitutional repeating units, not less than 80 % by weight of terephthalic acid unit based on the dicarboxylic acid component and not less than 80% by weight of ethylene glycol unit based on the glycol component, which is substantially free from scratches on the surface thereof and has a thickness uniformity of 1.0 to 10 %, a heat shrinkage of 0.05 to 0.6 % after the treatment at 120°C for 30 min, and a heat shrinkage of 0.1 to 0.7 % after the treatment at 150°C for 30 min. The polyethylene terephthalate (hereinafter abbreviated as PET) used in the present invention is a polyester in which 80 wt% or more of the acid component is constituted by terephthalic acid unit and 80 wt% or more of the glycol component is constituted by ethylene glycol unit. As other constituents of the acid component, there can be mentioned the units derived from a dicarboxylic acid such as oxalic acid, malonic acid, succinic acid, adipic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, naphthalenedicarboxylic acid and diphenyl ether dicarboxylic acid, and as other constituents of the glycol component there can be mentioned the unit derived from a diol such as propylene glycol, trimethylene glycol, tetramethylene glycol, hexamethylene glycol, diethylene glycol, triethylene glycol, polyalkylene glycol, 1,4-cyclohexanedimethanol and neopentyl glycol. In the present invention, a blend of two or more different types of polyesters can be used as PET as far as the content of terephthalic acid unit and that of ethylene glycol unit in the blend are 80 wt% or more of the total acid component and the total glycol component, respectively. PET used in the present invention may be added with phosphoric acid, phosphorous acid, their esters and inorganic particles (particles of silica, kaolin, calcium carbonate, calcium phosphate, titanium dioxide) at the stage of polymerization, or said inorganic particles, etc., may be blended in PET after polymerization. These materials are added in an amount of usually 0.01 to 30 wt% based on PET. The inorganic particles are preferably of a size falling within the range of 0.001 to 10 µm. A process for producing the thick polyester film in accordance with this invention will be described below. First, the PET is dried well, then melt extruded into a form of sheet through an extruder controlled at, for example, 280 to 290°C, a filter and a die, and then cast onto a rotating cooling drum kept at 10 to 70 °C, thereby effecting quick quenching and solidification to obtain a sheet. In this operation, it is preferred to contact the sheet closely to the drum by making use of electrostatic casting technique. This sheet is substantially in an amorphous state (the sheet in this state being hereinafter referred to as sheet A). In the present invention, the thickness of sheet A is 400 µm or greater, preferably 500 µm or greater, more preferably 800 µm or greater, further preferably 1,200 µm or greater. The sheet A is preheated to a temperature (surface temperature) of 50 to 130 °C by passing the sheet between or around a series of preheating rolls kept at 50 to 150 °C, and then, stretched in the machine direction in a single or multiple stages by a series of stretching rolls comprising a first set of nip rolls (slowest rolls) and at least one set of succeeding nip rolls (fast rolls). Each set of succeeding nip rolls is driven at a peripheral speed faster than the speed of the set of nip rolls located just before it, thereby effecting the stretching by the speed difference between the slower and faster sets of rolls. In this preheating and stretching operations, the preheating temperature and the film (sheet) surface temperature (T₁) at the point where the film parts from the surface of the slowest stretching nip rolls are so adjusted that the difference between the surface temperature (T₀) of the slowest stretching nip rolls and the stretching temperature (T), (T₀ - T), is -30 to 10°C, preferably -25 to 5°C, more preferably -20 to 0°C. If the difference exceeds 10°C, thickness uniformity of the final film will be impaired. The surface temperature (T₀) is preferably in the range of 70 to 90 °C. The stretch ratio in the machine direction (λ₁) is properly selected from the range of 1.2 to 4.0 times so that the index of birefringence (Δn₁) of the film after stretching will become 5.1 × 10⁻² or less. The stretching temperature (T) is equal to T₁ in the case where the stretching is conducted in a single stage. In the case of multiple-stage stretching, the stretching temperature (T) is represented by a weighted mean calculated from the following equation. For example, when the film is stretched 1.5 times at 85°C (film surface temperature at the point where the film parts from the surface of the first stretching nip rolls (slowest rolls)) and then further stretched 1.2 times at 90°C (film surface temperature at the point where the film parts from the surface of the second stretching rolls), the stretching temperature (T) is determined to be 87.2°C from the following equation. In the present invention, stretching is preferably conducted so that Δn₁ will become (75 - 0.625 × T) × 10⁻³ to (125 - 0.875 × T) × 10⁻³, when Δn₁ is less than (75 - 0.625 × T) × 10⁻³, film thickness may become non-uniform when the film is stretched in the transverse direction. On the other hand, when Δn₁ exceeds ( 125 - 0.875 × T) × 10⁻³, break of film occurs frequently when the film is stretched in the transverse direction. The obtained film, without being cooled to a temperature of glass transition point of the film or below, is again stretched 1.1 to 3.0 times (λ₂) either in a single stage or in multiple stages, preferably in the same series of stretching rolls as in the first stretching. The stretching temperature is 90 to 120°C, preferably 95 to 110°C, so that the index of birefringence Δn₂ after stretching will become 0.042 to 0.070, preferably 0.050 to 0.070, the stretching temperature being calculated in the same manner is in the first stretching. The film stretched at a temperature below 90°C or the film having an index of birefringence Δn₂ exceeding 0.070 tends to become relatively high in shrinkage in the machine direction after biaxial stretching. On the other hand, the film stretched at a temperature exceeding 120°C suffers an excess degree of crystallization, which causes frequent break of film at the time of stretching in the transverse direction or roughening of the film surface. on the other hand, the film with its index of birefringence less than 0.042 often proves to be non-uniform in thickness. In order to improve thickness uniformity of the film, it is preferred to perform the second machine-direction stretching at a stretching temperature lower than that of the first stretching. This measure proves particularly effective for improving thickness uniformity of thick films. The product of stretch ratios in the respective runs of stretching in the machine direction (overall stretch ratio in the machine direction) is in the range of 3.0 to 5.0 times. It is also preferred to properly select the stretching conditions so that the average refractive index n of the film after the second stretching in the machine direction will be in the range of 1.570 to 1.600. When n is less than 1.570, thickness uniformity is impaired, and when n exceeds 1.600, stretchability in the transverse direction is intolerably deteriorated. As for the material of the rolls used in the present invention, it is preferred that a silicone rubber coated roll and/or a fluorocarbon resin coated roll is used for at least the rolls at the end of a series of preheating rolls. When performing preheating of sheet A, it is preferred to use a hard chrome-plated roll until the film surface temperature reaches to 80°C, a ceramic roll until the film surface temperature reaches to 90°C and a silicone rubber coated rolls or a fluorocarbon resin coated roll for heating the film to a surface temperature of exceeding 90°C. In the present invention, ceramic rolls are preferably used as the stretching rolls. When producing a stretched film having a thickness of 25 µm or greater as in the present invention, a large stretching stress may arise, and therefore, the silicone rubber coated roll and the fluorocarbon resin coated roll are not preferred because of their poor wear resistance. For further reducing the risk of scratching of the film surface by the rolls, the ceramic rolls are preferred so designed as to have a surface roughness (Rmax) of not more than 1 µm, preferably not more than 0.8 µm It is also possible to prevent scratching or scuffing by stretching the film without winding it on the rolls but by nipping it by the rolls so as to minimize the contact area between the film and each roll. The film which has been stretched in the machine direction in the manner described above is then further stretched 3.2 to 5.0 times, preferably 3.5 to 4.0 times, in the transverse direction in a tenter to give a biaxially stretched film. This transverse stretching is conducted at a temperature of 95 to 140°C. The thus obtained biaxially stretched film may be immediately subjected to a heat treatment at 130 to 250°C, but if necessary for meeting the specific property requirements, the stretched film may be relaxed 0.5 to 10 % in the transverse direction in the course of heat treatment, or may be relaxed 0.05 to 3 % in the machine direction and/or transverse direction after the heat treatment but before being wound onto a windup roll. A coating layer may be formed on one or both surfaces of the polyester film of this invention by in-line coating method for providing the film with surface properties such as adhesiveness, releasability, antistatic properties, slipperiness, which are required according to the purpose of use of the film. The biaxially stretched polyester film produced by the method of the present invention described above is substantially free from scratches (no scratch is noticed on the film surface by naked eye in fluorescent light) and has a thickness uniformity of 1.0 to 10 %, preferably 1.0 to 8.0 %, a heat shrinkage of 0,05 to 0.6%, preferably 0.05to 0.5 % after the treatment at 120°C for 30 min, a heat shrinkage of 0.1 to 0.7 %, preferably 0.1 to 0.6% after the treatment at 150°C for 30 min. The thickness of the biaxially stretched film obtained according to the process of this invention is in the range of 25 to 500 µm. The biaxially stretched polyester film produced according to the present invention can be applied to various use, but it finds particularly useful as films for touch panels, and membrane switches. Thus, the present invention is of high industrial utility. The present invention will hereinafter be described in further detail by showing the examples thereof, but it is to be understood that these examples are merely intended to be illustrative and not to be construed as limiting the scope of the invention. The methods used for determining the film properties are as described below. (1) Heat shrinkage ( machine direction) Each of the strip film samples was heat treated under a tension-free state in an atmosphere of 120°C or 150°C for 30 minutes, and the length of each of the samples before and after the heat treatment was measured, and the heat shrinkage of the film was determined from the following formula: (2) Thickness uniformity Thickness in the machine direction of each sample of biaxially stretched film was measured by a continuous film thickness meter (using an electron micrometer) mfd. by Anritsu Denki Co., Ltd., and film thickness uniformity along the length of 15 meters was calculated from the following formula: (3) Film surface temperature Measured by using a Burns' thermometer. (4) Index of birefringence Measured by using an Abbe's refractometer. (5) Flatness The appearance of the film was observed visually and estimated according to the following ratings. o ○ : excellent ○ : good with no emboss and wrinkle. ▵ : emboss or wrinkle was noticed under careful observation. X : a lot of emboss or wrinkle. (6) Scratch on the film surface The appearance of the film was observed visually or under a microscope in fluorescent light and estimated according to the following ratings. ○ : no scratch was noticed. ▵ : no scratch was noticed by naked eye, but slightly noticed under a microscope. X : scratch was noticed by naked eye. XX : scratch was clearly noticed by naked eye. In the following Examples and Comparative Examples, all "parts" are by weight unless otherwise noted. EXAMPLES 1, 2 and 3 Preparation of polyester chips 100 parts of dimethyl terephthalate, 70 parts of ethylene glycol and 0.07 part of calcium acetate monohydrate were supplied into a reactor and heated therein while evaporating away methanol. The mixture was heated to 230°C over a period of 4.5 hours after start of the reaction to substantially complete the ester exchange reaction. The reaction mixture was then further added with 0.04 part of phosphoric acid and 0.035 part of antimony trioxide and polymerized by a conventional method. That is, the reaction temperature was gradually raised till reaching finally 280°C while pressure was gradually reduced to 66.6 Pa (0.5 mmHg). The reaction was completed in 4 hours, and the reaction product was made into chips in a usual way to obtain a polyester (A). Separately from the above operations, there was obtained an amorphous silica-containing polyester (B) by following the same process as preparation of polyester (A) except that 0.13 part of amorphous silica having an average particle size of 1.2 µm was added after the end of ester exchange reaction. There was also obtained an amorphous silica-containing polyester (C) in the same way as preparation of polyester (B) except for use of amorphous silica having an average particle size of 30 µm in an amount of 0.05 part. Production of film The polyester (A), polyester (B) and polyester (C) were blended in a ratio of 60 : 15 : 25, and the blend was air dried at 180°C for 4 hours, melt extruded at 285°C and cooled and solidified on a casting drum to obtain an amorphous sheet. In the cooling and solidifying operation, the film was attached closely to the drum by using a conventional electrostatic casting method, The thickness of the obtained unstretched film is shown in Table 1. The unstretched film was first preheated by three hard chrome-plated rolls, 150 mm in diameter, kept at 60 to 75°C, further preheated by five ceramic rolls, 150 mm in diameter, kept at 80 to 90°C, and then additionally preheated by seven PFA (tetrafluoroethylene-perfluoroalky/vinyl ether copolymer) rolls, 150 mm in diameter, kept at 91 to 110°C. The preheated film was guided to the ceramic stretching rolls kept at 85°C and thereby stretched 1.5 times at 105°C and 2.0 times at 100°C. The index of birefringence Δn₁ of the obtained film was 0.030. Then this film, without being cooled to T g or below, was further stretched 1.3 times (EXAMPLE 1), 1.4 times (EXAMPLE 2) and 1.5 times (EXAMPLE 3) in the machine direction at 97°C to obtain the films having an index of birefringence after machine-direction stretching (Δn₂) of 0.048 (EXAMPLE 1), 0.055 (EXAMPLE 2) and 0.067 (EXAMPLE 3). These films were then stretched 3.5 times in the transverse direction at 110°C and heat set at 242°C to obtain the films having a thickness of 100 µm. The properties of the obtained films and their evaluation results are shown in Table 1. COMPARATIVE EXAMPLES 1 to 3 An unstretched film was made by using the same materials as employed in Examples described above, and this unstretched film was preheated by three hard chrome-plated rolls kept at 60 to 70°C, further preheated by two ceramic rolls kept at 80 to 95°C, and then stretched by ceramic rolls of 93°C. In this treatment, roll surface temperature T₀ was 93°C and film surface temperature T₁ was 82°C. When two samples of this film were biaxially stretched so that Δn₁ would become 0.050 (Comparative Example 1) and 0.070 (Comparative Example 2), respectively, each of the obtained films had cross-stripes and were also poor in thickness uniformity. When preheating temperature and stretching roll temperature were raised to 90 to 105°C and 103°C to stretch at a higher temperature (the film surface temperature) of 90°C, the film adhered to the rolls, causing non-uniformity of film thickness. Thus, the obtained film was a defective one. Also, when a biaxially stretched film with Δn₁ of 0.105 was produced (Comparative Example 3), the obtained film, although having satisfactory flatness and thickness uniformity, showed a very large shrinkage.

Claims: A process for producing a biaxially stretched polyester film of 25 to 500 µm thickness, the film being substantially free from scratches on the surface thereof and having a low shrinkage, a uniform thickness and an improved flatness, which comprises the steps of: extruding a molten polyester resin comprising, as the constitutional repeating units, not less than 80 % by weight of terephthalic acid unit based on the dicarboxylic acid component and not less than 80% by weight of ethylene glycol unit based on the glycol component onto a cooling drum to cool and solidify the molten polyester resin thereby forming a substantially amorphous sheet having a thickness of 400 µm or greater; preheating the sheet to a surface temperature of 50 to 130 °C by passing the sheet between or around a series of preheating rolls; stretching the preheated sheet 1.2 to 4.0 times in the machine direction in a single or multiple stages by a series of stretching rolls comprising a set of the slowest nip rolls and at least one set of succeeding nip rolls at a stretching temperature of 85 to 120 °C, by maintaining the difference between the surface temperature of the slowest nip rolls and the stretching temperature from -30 to 10 °C, so that the resultant stretched film has an index of birefringence of 5.1 x 10⁻² or less, the stretching temperature (T) being represented by the following formula: further stretching the film 1.1 to 3.0 times in the machine direction in a single or multiple stages by a series of stretching rolls comprising at least two sets of nip rolls at a stretching temperature of 90 to 120 °C without cooling the film to a temperature of the glass transition point of the film or less, so that the overall stretch ratio in the machine direction is in the range of 3.0 to 5.0 times and the resultant stretched film has an index of birefringence of 0.042 to 0.70, the stretching temperature being represented by the same formula as in the first stretching; stretching the thus stretched film 3.2 to 5.0 times in the transverse direction at a temperature of 95 to 140 °C; and subjecting the biaxially stretched film to a heat treatment at a temperature of 130 to 250 °C with or without 0.5 to 10 % relaxation in the transverse direction. The process according to claim 1, wherein at least a set of rolls at the end of the series of preheating rolls are a silicon rubber coated roll and/or a fluorcarbon resin coated roll. The process according to claim 1, wherein the stretching rolls are ceramic rolls. The process according to claim 1, wherein the second stretching in the machine direction is conducted at a stretching temperature lower than the stretching temperature of the first stretching. The process according to claim 1, wherein the heat-treated film is further subjected to 0.05 to 3 % relaxation in the machine direction and/or transverse direction after the heat treatment but before being wound onto a windup roll.

Inventors: FUKUDA YUJIRO C O DIAFOIL AMER, MIKI TAKATOSHI, TOMITAKA KICHINOJO, UTSUMI SHIGEO, FUKUDA, YUJIRO, C/O DIAFOIL AMERICA INC., MIKI, TAKATOSHI, TOMITAKA, KICHINOJO, UTSUMI, SHIGEO
Applicants: DIAFOIL HOECHST CO LTD, DIAFOIL HOECHST CO., LTD
Application year: 1990
Main classification: C08J5
IPC codes: C08J5, B29L7, B29C55, B29K67