JP4609580B2 - Manufacturing method of polyester film for molding - Google Patents

Description

The present invention is excellent in moldability, transparency, solvent resistance, heat resistance under low temperature and low pressure, and blocking or film breakage occurs when unwinding a long film wound up in a roll shape. In addition, the present invention relates to a molding polyester film suitable for use as a casing for various portable devices or a member thereof, a member for a name plate or a member for a building material of a home appliance or an automobile, which has a smaller environmental load. In addition, the present invention relates to a polyester film for molding that is excellent in light resistance suitable for applications used outdoors (members for automobile exteriors or building materials).
Furthermore, it is related with the film for shaping | molding which provided the hard-coat layer which is excellent in a moldability and is excellent in abrasion resistance.

  Conventionally, as a sheet | seat for shaping | molding, a polyvinyl chloride film is typical and has been preferably used at points, such as workability. On the other hand, the film has problems such as generation of toxic gas when the film burns due to fire and the like, bleed-out of the plasticizer, and the recent demand for environmental resistance has demanded new materials with low environmental impact. ing.

In order to satisfy the above requirements, unstretched sheets made of polyester, polycarbonate and acrylic resin have been used in a wide range of fields as non-chlorine materials. In particular, unstretched sheets made of a polyester resin are attracting attention because they have good mechanical properties and transparency, and are excellent in economic efficiency. For example, an unstretched polyester-based sheet comprising substantially non-crystalline polyester-based resin in which about 30 mol% of ethylene glycol component in polyethylene terephthalate is substituted with 1,4-cyclohexanedimethanol is disclosed ( For example, see Patent Documents 1 to 5).
Japanese Patent Laid-Open No. 9-156267 JP 2001-71669 A JP 2001-80251 A JP 2001-129951 A JP 2002-249652 A

  The above-mentioned unstretched polyester sheet satisfies market demands regarding moldability and laminate suitability, but because it is an unstretched sheet, it does not have sufficient heat resistance and solvent resistance and satisfies high market demands. It has not yet reached.

As a method for solving the above problems, a method using a biaxially stretched polyethylene terephthalate film is disclosed (for example, see Patent Documents 6 to 9).
JP-A-9-187903 JP-A-10-296937 Japanese Patent Laid-Open No. 11-10816 JP-A-11-268215

  However, although the heat resistance and solvent resistance are improved, the above method has insufficient moldability and does not satisfy the market demand in terms of the balance of overall quality.

As a method for solving the above-described problem, a method for specifying a stress at 100% elongation of a film is disclosed (for example, see Patent Documents 10 and 11).
JP-A-2-204020 JP 2001-347565 A

  Although this method has improved moldability as compared with the above-described method, it does not reach a level that can sufficiently meet the high demands of the market regarding moldability. In particular, there remains a problem in moldability that can be adapted to lowering the molding temperature and the finished quality of the obtained molded product.

The present inventors have studied the solution of the above-mentioned problem, and have already developed a method of improving the above-mentioned problem by specifying a 100% elongation stress of the film using a copolymer polyester resin having the specified composition as a raw material. (For example, refer to Patent Document 11).
Japanese Patent Application Laid-Open No. 2004-075713

  With this method, in the mold molding method with high molding pressure at the time of molding, it can greatly improve the moldability that can meet the market demand and adapt to the lowering of the molding temperature and the finished product obtained. it can. However, in the case of a molding method having a low molding pressure at the time of molding, such as a compressed air molding method or a vacuum molding method, which has become increasingly demanding in the market, it is desired to further improve the finish of the molded product.

In addition, as a polyester film for molding that can be applied to a pressure molding method or a vacuum molding method, which is a molding method with a low molding pressure at the time of molding, it is composed of a biaxially stretched polyester film containing a copolymerized polyester, and the film at 25 ° C and 100 ° C The present inventors have proposed a polyester film for molding having a specific range of stress at 100% elongation, storage elastic modulus (E ′) at 100 ° C. and 180 ° C., and thermal deformation rate at 175 ° C. (for example, Patent Document 13) reference). However, it was found that blocking and tearing are likely to occur when the film is continuously produced and wound into a roll, and then the film is unwound and processed. Therefore, it is desired to further improve the productivity and the stability of quality during post-processing such as deposition or sputtering of metal or metal oxide on a film or printing.
JP-A-2005-290354

  The object of the present invention is to solve the above-mentioned conventional problems, and is excellent in moldability, transparency, solvent resistance, and heat resistance at low temperature and low pressure, and is wound in a roll shape. Polyester for molding that is suitable for use as a housing for various portable devices, members for nameplates or building materials for home appliances and automobiles, which does not cause blocking or film breakage when unwinding a long film and has a low environmental impact To provide a film.

The manufacturing method of the polyester film for shaping | molding of this invention which can solve said subject consists of the following structures.

1st invention in this invention is a manufacturing method of the polyester film for shaping | molding which satisfy | fills the requirements of following (1)-(6) consisting of the biaxially-oriented polyester film containing copolyester, Comprising: The heat | fever after biaxial stretching In the fixing process, the heat treatment is performed in two or more stages, and the first stage heat treatment temperature (TS1) is in the range of −5 ° C. to −30 ° C. of the second stage heat treatment temperature (TS2). the heat treatment temperature (TS2) is characterized in that in a range of -5 ° C. ~ - 35 ° C. of the melting point of the film, a manufacturing method of molding a polyester film. (1) The copolymer polyester comprises (a) an aromatic dicarboxylic acid component, ethylene glycol, and a copolymer polyester composed of a glycol component containing a branched aliphatic glycol or alicyclic glycol as a copolymer component, or ( b) Consists of an terephthalic acid and an aromatic dicarboxylic acid component containing isophthalic acid as a copolymer component, and a glycol component containing ethylene glycol. (2) The content of the copolymer component in the copolymer polyester is 5 to 50. Mol%, (3) (a) containing particles in the film, or (b) the film containing substantially no particles and containing particles only in the surface layer, (4) 150 of the film The thermal shrinkage in the longitudinal direction and the width direction at 0.01 ° C. is 0.01 to 5.0%, (5) haze is 0.1 to 3.0%, (6) at least The surface roughness of the surface of the film (Ra) is 0.005～0.030Myuemu,

2nd invention is the manufacturing method of the said polyester film for shaping | molding characterized by the heat processing temperature (TS2) of the said 2nd step being the highest heat processing temperature in a heat setting process.

3rd invention is a manufacturing method of the said polyester film for shaping | molding characterized by the said polyester film for shaping | molding further satisfy | filling the following (7)-(10) requirements. (7) 100% elongation stress in the longitudinal direction and width direction of the film is 40 to 300 MPa at 25 ° C. and 1 to 100 MPa at 100 ° C., (8) The branched aliphatic glycol is neopentyl glycol, the fat It is 1,4-cyclohexanedimethanol which is a cyclic glycol, (9) the melting point of the film is 200 to 245 ° C., and (10) the degree of plane orientation is 0.095 or less.

4th invention is the average particle diameter of 0.01-10 micrometers of the particle | grains contained in the said surface layer, The particle | grain content in the said surface layer is 0.01-25 mass%, The said for molding characterized by the above-mentioned It is a manufacturing method of a polyester film.

  The molding polyester film of the present invention is excellent in moldability at the time of heat molding at a low temperature or low pressure, and therefore can be applied to a wide variety of molding methods, and when used in a room temperature atmosphere as a molded product, Excellent in shape stability (heat shrinkage characteristics, thickness unevenness), solvent resistance, heat resistance, and environmental impact is small. Further, when unwinding a long film wound up in a roll shape at the time of post-processing, blocking and tearing are unlikely to occur, resulting in excellent productivity. Furthermore, since the smoothness and transparency are highly excellent, it is excellent in design when a vapor deposition layer, a sputtering layer, or a printing layer is provided during post-processing. Therefore, it is suitable as a casing of various portable devices or a member thereof, a member for a nameplate or a member for building material of home appliances or automobiles.

  In addition, by incorporating an ultraviolet absorber in the film and reducing the transmittance in the ultraviolet region, light resistance can be imparted, particularly for applications used outdoors (members for automobile exteriors or building materials). It is suitable as a molding material.

  First, the technical significance of the physical properties defined by the moldable polyester film of the present invention will be described. Next, a method for producing the moldable polyester film of the present invention will be described.

(Technical meaning and significance of physical properties described in the present invention)
In the present invention, the stress at 100% elongation (F100) is a measure closely related to the moldability of the film. The reason why F100 is closely related to the moldability of the film is, for example, when a biaxially oriented polyester film is molded using a vacuum forming method, the film locally expands to 100% or more near the corner of the mold. There is a case. In a film having a high F100, extremely high stress is partially generated in such a locally stretched portion, and it is considered that the film breaks due to the stress concentration and the formability is lowered. On the other hand, a film having an F100 that is too small has good moldability, but only a very weak tension is generated in a portion that is uniformly stretched, such as a flat portion of a mold. It is thought that proper elongation cannot be obtained.

In the present invention, 100% elongation stress (F100 ₁₀₀ ) at 100 ° C. is used as a physical property related to the moldability corresponding to the temperature at the time of molding. In addition, when molding using a mold having irregularities and depressions, 100% at 25 ° C. is a physical property related to the moldability when the film before molding is lightly followed by the mold before molding. Elongation stress (F100 ₂₅ ) is used.

The polyester film for molding in the present invention has a stress at 100% elongation (F100 ₂₅ ) at 25 ° C. in the longitudinal direction and the width direction of the film of 30 to 300 MPa.

F100 ₂₅ in the longitudinal direction and the width direction of the film is 40 to 300 MPa, and the lower limit is preferably 50 MPa, more preferably 60 MPa. The upper limit is preferably 250 MPa, more preferably 200 MPa, and still more preferably 180 MPa. When F100 ₂₅ is less than 40 MPa, when the roll-shaped film is pulled and unwound, the film is stretched or torn, resulting in poor workability. On the other hand, when F100 ₂₅ exceeds 300 MPa, the moldability becomes poor. In particular, when molding is performed using a mold having irregularities and depressions, a film before molding may be followed by lightly following those molds in advance. In such a case, it is difficult to mold the film, and the finished product may have poor design properties.

In the molding polyester film of the present invention, it is important that the 100% elongation stress (F100 ₁₀₀ ) at 100 ° C. in the longitudinal direction and the width direction of the film is _{1 to 100} MPa.

The upper limit of F100 ₁₀₀ in the longitudinal direction and the width direction of the film is preferably 90 MPa, more preferably 80 MPa, and particularly preferably 70 MPa from the viewpoint of moldability. On the other hand, the lower limit of F100 ₁₀₀ is preferably 5 MPa, more preferably 10 MPa, and particularly preferably 20 MPa from the viewpoint of elasticity and shape stability when using a molded product.

  In the film of the present invention, the thermal shrinkage in the longitudinal direction and the width direction at 150 ° C. is 0.01 to 5.0%. The lower limit value of the heat shrinkage rate at 150 ° C. is preferably 0.1%, more preferably 0.5%. On the other hand, the upper limit value of the heat shrinkage rate at 150 ° C. is preferably 4.5%, more preferably 4.1%, and still more preferably 3.2%. Even when a biaxially stretched polyester film for molding having a thermal shrinkage of less than 0.01% in the longitudinal and width direction films at 150 ° C. is produced, there is no significant difference in practical effects, and productivity is improved. Since it is very low, there is no necessity to make the heat shrinkage rate at 150 ° C. less than 0.01%. On the other hand, if the thermal shrinkage rate of the film in the longitudinal direction and the width direction at 150 ° C. exceeds 5.0%, the film is likely to be deformed in a post-processing step that requires heat such as vapor deposition, sputtering or printing, and after post-processing. The appearance and design of the film will be poor.

  In the present invention, the haze of the film is 0.1 to 3.0%. The lower limit of haze is preferably 0.3%, more preferably 0.5%. On the other hand, the upper limit of haze is preferably 2.5%, more preferably 2.0%. A film having a haze of less than 0.1% is poor in slipperiness, so that it is difficult to produce it on an industrial scale with normal productivity. On the other hand, when the haze of the film exceeds 3.0%, when the vapor deposition or sputtering surface of the metal or the printed surface is viewed from the back surface of the film, the metal or the printed surface looks dull, resulting in poor design. In addition, it is difficult to obtain a film having a haze of 2.0% or less by a method for forming irregularities on the film surface by incorporating particles in the film, which is generally performed for improving handling properties in the film. .

  In the present invention, the surface roughness (Ra) of at least one film is 0.005 to 0.030 μm. The lower limit of Ra is preferably 0.006 μm, and more preferably 0.007 μm. On the other hand, the upper limit value of Ra is preferably 0.025 μm, more preferably 0.015 μm. As the Ra of at least one side of the film becomes smaller, it becomes difficult to wind the film, and the frequency of occurrence of blocking or breaking of the film increases when the film once wound up in a roll shape is unwound. On the other hand, when Ra exceeds 0.03 μm, the protrusion becomes a defect in a post-processing step such as vapor deposition, sputtering, or printing, and the design property is deteriorated.

  In the present invention, the degree of plane orientation (ΔP) of the film is also a physical property related to moldability, and the higher the degree of plane orientation, the more the molecular chains are arranged in the plane direction and the moldability is lowered. In the present invention, the plane orientation degree of the film is 0.095 or less. The upper limit of the degree of plane orientation is preferably 0.090. Further, the smaller the degree of plane orientation, the better the moldability, but the strength of the film is lowered, and the flatness such as thickness unevenness tends to deteriorate. Therefore, the lower limit of the degree of plane orientation is preferably 0.001, more preferably 0.01, and particularly preferably 0.04.

(Concept of the present invention)
This application is an improved invention of Patent Document 12 described in the prior art.
A polyester film obtained by using a copolymer polyester containing 5 to 50 mol% of a copolymer component as a raw material as in the present invention has a slower crystallization rate and lower crystallinity than a polyethylene terephthalate film or the like. In order to reduce the degree of plane orientation and the thermal shrinkage at 150 ° C., when the method of heat treatment at a higher temperature than usual described in Patent Document 12 is used, the heat treatment is suddenly performed at a high temperature after completion of stretching. In the heat treatment zone, the mobility of molecules constituting the material having low crystallinity is increased. Therefore, the surface protrusions formed by the bulging of the particles (particles in the biaxially oriented film or particles in the coating layer) in the stretching process are buried again in the heat treatment zone, so that the surface roughness is sufficient. Can't get. Therefore, there is a problem that haze deteriorates when the amount of particles added is increased more than necessary in order to prevent the blocking and tearing when winding the film neatly and winding the film wound up in a roll shape. .

  In the present invention, the above-mentioned problems have been solved by using a suitable method in which the heat treatment zone has two stages (or more) and the first stage heat treatment temperature TS1 and the second stage heat treatment temperature TS2 are controlled within a specific range. It is. This mechanism is considered as follows.

  In the first heat treatment zone, the crystallization of the film is promoted to some extent before the particles are buried inside the film, and even if the temperature is raised sufficiently in the second heat treatment zone, the molecular motion The properties are sufficiently lowered, and the film having a low thermal shrinkage rate can be obtained by further promoting the crystallinity while forming the projections on the surface. Moreover, it is not necessary to contain particles more than necessary from the viewpoint of transparency.

(Preferable production method of film)
The polyester film for molding of the present invention uses a copolymerized polyester as a raw material. Examples of the copolyester include (a) a copolyester composed of an aromatic dicarboxylic acid component, ethylene glycol, and a glycol component containing a branched aliphatic glycol or alicyclic glycol, or (b) terephthalic acid and isophthalic acid. A copolyester composed of an aromatic dicarboxylic acid component containing an acid and a glycol component containing ethylene glycol is preferred. Moreover, it is preferable from the point which further improves the moldability that the polyester which comprises a biaxially-oriented polyester film further contains a 1, 3- propanediol unit or a 1, 4- butanediol unit as a glycol component.

  In the present invention, as the film raw material, any method of copolymerized polyester alone, one or more homopolyesters or a blend of copolymerized polyesters, or a combination of homopolyester and copolymerized polyester is possible. Among these, the blending method is preferable from the viewpoint of suppressing the lowering of the melting point.

  When using a copolymer polyester composed of an aromatic dicarboxylic acid component, ethylene glycol, and a glycol component containing a branched aliphatic glycol or alicyclic glycol as the copolymer polyester, the aromatic dicarboxylic acid component is Terephthalic acid, isophthalic acid, naphthalene dicarboxylic acid or ester-forming derivatives thereof are preferred, and the amount of terephthalic acid and / or naphthalene dicarboxylic acid component relative to the total dicarboxylic acid component is 70 mol% or more, preferably 85 mol% or more. Particularly preferred is 95 mol% or more, and particularly preferred is 100 mol%.

  Examples of branched aliphatic glycols include neopentyl glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, and the like. Examples of the alicyclic glycol include 1,4-cyclohexanedimethanol and tricyclodecane dimethylol.

  Among these, neopentyl glycol and 1,4-cyclohexanedimethanol are particularly preferable. Furthermore, in the present invention, it is a more preferable embodiment that 1,3-propanediol or 1,4-butanediol is used as a copolymerization component in addition to the glycol component. Use of these glycols as a copolymerization component is suitable for imparting the above-mentioned properties, and is also excellent in transparency and heat resistance, and from the viewpoint of improving the adhesion with the adhesion modified layer. Is also preferable.

  When the copolymer polyester is composed of an aromatic dicarboxylic acid component containing terephthalic acid and isophthalic acid and a glycol component containing ethylene glycol, the amount of ethylene glycol is based on the total glycol component. It is 70 mol% or more, preferably 85 mol% or more, particularly preferably 95 mol% or more, and particularly preferably 100 mol%. As the glycol component other than ethylene glycol, the above-mentioned branched aliphatic glycol, alicyclic glycol, or diethylene glycol is preferable.

  Examples of the catalyst used for producing the copolymer polyester include alkaline earth metal compounds, manganese compounds, cobalt compounds, aluminum compounds, antimony compounds, titanium compounds, titanium / silicon composite oxides, and germanium compounds. . Of these, titanium compounds, antimony compounds, germanium compounds, and aluminum compounds are preferred from the viewpoint of catalytic activity.

  When producing the copolymer polyester, it is preferable to add a phosphorus compound as a heat stabilizer. As said phosphorus compound, phosphoric acid, phosphorous acid, etc. are preferable, for example.

  The copolyester preferably has an intrinsic viscosity of 0.50 dl / g or more, more preferably 0.55 dl / g or more, and particularly preferably from the viewpoint of moldability, adhesion, and film formation stability. 60 dl / g or more. If the intrinsic viscosity is less than 0.50 dl / g, the moldability tends to decrease. In addition, when a filter for removing foreign substances is provided in the melt line, the upper limit of the intrinsic viscosity is preferably 1.0 dl / g from the viewpoint of ejection stability during extrusion of the molten resin.

  In the present invention, one or more homopolyesters or copolymerized polyesters are used as film raw materials, and these are blended to form a film, thereby maintaining the same flexibility as when only the copolymerized polyester is used. However, transparency and high melting point (heat resistance) can be realized. In addition, when only a high melting point homopolyester (for example, polyethylene terephthalate) is used, it is possible to realize a melting point (heat resistance) having no flexibility and practical problem while maintaining high transparency.

  Further, blending at least one or more of the copolymer polyester and a homopolyester other than polyethylene terephthalate (for example, polytetramethylene terephthalate or polybutylene terephthalate) and using it as a raw material for the molding polyester film of the present invention, It is further preferable from the viewpoint of moldability.

  The melting point of the polyester film is preferably 200 to 245 ° C. from the viewpoint of heat resistance and moldability. By controlling the type and composition of the polymer to be used and the film forming conditions within the range of the melting point, a balance between moldability and finish can be achieved, and a high-quality molded product can be produced economically. Here, the melting point is an endothermic peak temperature at the time of melting, which is detected at the time of primary temperature rise in so-called differential scanning calorimetry (DSC). The melting point was determined by measuring using a differential scanning calorimeter (manufactured by Mac Science, DSC3100S) at a heating rate of 20 ° C./min. The lower limit of the melting point is more preferably 210 ° C, particularly preferably 230 ° C. If the melting point is less than 200 ° C, the heat resistance tends to deteriorate. Therefore, it may become a problem when exposed to high temperature during molding or use of a molded product.

  The molding polyester film of the present invention preferably has a light transmittance of 50% or less at a wavelength of 370 nm, more preferably 40% or less, and particularly preferably 30% or less. By controlling the light transmittance at a wavelength of 370 nm of the polyester film for molding to 50% or less, the light resistance of the printed layer is improved particularly when the film is printed.

  As a method of controlling the light transmittance at a wavelength of 370 nm to 50% or less, a method of blending an ultraviolet absorber in any of the constituent layers of the molding polyester film is used. The ultraviolet absorber may be either inorganic or organic as long as it can impart the above characteristics. Examples of organic ultraviolet absorbers include benzotoazole, benzophenone, cyclic imino ester, and combinations thereof. From the viewpoint of heat resistance, benzotoazole and cyclic imino ester are preferred. When two or more kinds of ultraviolet absorbers are used in combination, ultraviolet rays having different wavelengths can be absorbed simultaneously, so that the ultraviolet absorption effect can be further improved.

  Examples of the benzotriazole ultraviolet absorber include 2- [2′-hydroxy-5 ′-(methacryloyloxymethyl) phenyl] -2H-benzotriazole and 2- [2′-hydroxy-5 ′-(methacryloyloxyethyl). ) Phenyl] -2H-benzotriazole, 2- [2'-hydroxy-5 '-(methacryloyloxypropyl) phenyl] -2H-benzotriazole, 2- [2'-hydroxy-5'-(methacryloyloxyhexyl) phenyl ] -2H-benzotriazole, 2- [2'-hydroxy-3'-tert-butyl-5 '-(methacryloyloxyethyl) phenyl] -2H-benzotriazole, 2- [2'-hydroxy-5'-tert -Butyl-3 '-(methacryloyloxyethyl) phenyl] -2 -Benzotriazole, 2- [2'-hydroxy-5 '-(methacryloyloxyethyl) phenyl] -5-chloro-2H-benzotriazole, 2- [2'-hydroxy-5'-(methacryloyloxyethyl) phenyl] -5-methoxy-2H-benzotriazole, 2- [2'-hydroxy-5 '-(methacryloyloxyethyl) phenyl] -5-cyano-2H-benzotriazole, 2- [2'-hydroxy-5'-( Methacryloyloxyethyl) phenyl] -5-tert-butyl-2H-benzotriazole, 2- [2′-hydroxy-5 ′-(methacryloyloxyethyl) phenyl] -5-nitro-2H-benzotriazole, and the like. However, it is not particularly limited to these.

  Examples of the cyclic imino ester UV absorber include 2,2 ′-(1,4-phenylene) bis (4H-3,1-benzoxazin-4-one), 2-methyl-3,1-benzoxazine. -4-one, 2-butyl-3,1-benzoxazin-4-one, 2-phenyl-3,1-benzoxazin-4-one, 2- (1- or 2-naphthyl) -3,1- Benzoxazin-4-one, 2- (4-biphenyl) -3,1-benzoxazin-4-one, 2-p-nitrophenyl-3,1-benzoxazin-4-one, 2-m-nitrophenyl -3,1-benzoxazin-4-one, 2-p-benzoylphenyl-3,1-benzoxazin-4-one, 2-p-methoxyphenyl-3,1-benzoxazin-4-one, 2- o-methoxy Enyl-3,1-benzoxazin-4-one, 2-cyclohexyl-3,1-benzoxazin-4-one, 2-p- (or m-) phthalimidophenyl-3,1-benzoxazin-4-one 2,2 ′-(1,4-phenylene) bis (4H-3,1-benzoxazinon-4-one) 2,2′-bis (3,1-benzoxazin-4-one), 2, 2′-ethylenebis (3,1-benzoxazin-4-one), 2,2′-tetramethylenebis (3,1-benzoxazin-4-one), 2,2′-decamethylenebis (3 1-benzoxazin-4-one), 2,2′-p-phenylenebis (3,1-benzoxazin-4-one), 2,2′-m-phenylenebis (3,1-benzoxazine-4) -On), 2,2 '-(4,4 '-Diphenylene) bis (3,1-benzoxazin-4-one), 2,2'-(2,6- or 1,5-naphthalene) bis (3,1-benzoxazin-4-one), 2 , 2 ′-(2-methyl-p-phenylene) bis (3,1-benzoxazin-4-one), 2,2 ′-(2-nitro-p-phenylene) bis (3,1-benzoxazine- 4-one), 2,2 ′-(2-chloro-p-phenylene) bis (3,1-benzoxazin-4-one), 2,2 ′-(1,4-cyclohexylene) bis (3 1-benzoxazin-4-one) 1,3,5-tri (3,1-benzoxazin-4-on-2-yl) benzene, 1,3,5-tri (3,1-benzoxazine-4 -On-2-yl) naphthalene and 2,4,6-tri (3,1-ben Oxazin-4-on-2-yl) naphthalene, 2,8-dimethyl-4H, 6H-benzo (1,2-d; 5,4-d ′) bis- (1,3) -oxazine-4,6 -Dione, 2,7-dimethyl-4H, 9H-benzo (1,2-d; 5,4-d ') bis- (1,3) -oxazine-4,9-dione, 2,8-diphenyl- 4H, 8H-benzo (1,2-d; 5,4-d ′) bis- (1,3) -oxazine-4,6-dione, 2,7-diphenyl-4H, 9H-benzo (1,2 -D; 5,4-d ') bis- (1,3) -oxazine-4,6-dione, 6,6'-bis (2-methyl-4H, 3,1-benzoxazin-4-one) 6,6′-bis (2-ethyl-4H, 3,1-benzoxazin-4-one), 6,6′-bis (2-phenyl-4) H, 3,1-benzoxazin-4-one), 6,6′-methylenebis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,6′-methylenebis (2-phenyl-) 4H, 3,1-benzoxazin-4-one), 6,6′-ethylenebis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,6′-ethylenebis (2- Phenyl-4H, 3,1-benzoxazin-4-one), 6,6′-butylenebis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,6′-butylenebis (2- Phenyl-4H, 3,1-benzoxazin-4-one), 6,6′-oxybis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,6′-oxybis (2- Phenyl-4H, 3,1-benzooxy Din-4-one), 6,6′-sulfonylbis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,6′-sulfonylbis (2-phenyl-4H, 3,1) -Benzoxazin-4-one), 6,6'-carbonylbis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,6'-carbonylbis (2-phenyl-4H, 3 , 1-benzoxazin-4-one), 7,7′-methylenebis (2-methyl-4H, 3,1-benzoxazin-4-one), 7,7′-methylenebis (2-phenyl-4H, 3 , 1-benzoxazin-4-one), 7,7′-bis (2-methyl-4H, 3,1-benzoxazin-4-one), 7,7′-ethylenebis (2-methyl-4H, 3,1-benzoxazin-4-one), , 7′-oxybis (2-methyl-4H, 3,1-benzoxazin-4-one), 7,7′-sulfonylbis (2-methyl-4H, 3,1-benzoxazin-4-one), 7,7′-carbonylbis (2-methyl-4H, 3,1-benzoxazin-4-one), 6,7′-bis (2-methyl-4H, 3,1-benzoxazin-4-one) 6,7′-bis (2-phenyl-4H, 3,1-benzoxazin-4-one), 6,7′-methylenebis (2-methyl-4H, 3,1-benzoxazin-4-one) And 6,7'-methylenebis (2-phenyl-4H, 3,1-benzoxazin-4-one).

  When blending the above-mentioned organic ultraviolet absorber into a film, it is exposed to a high temperature in the extrusion process. Therefore, it is necessary to use an ultraviolet absorber having a decomposition start temperature of 290 ° C. or higher as a process contamination during film formation. It is preferable in order to reduce it. If an ultraviolet absorber having a decomposition start temperature of 290 ° C. or lower is used, the decomposed product of the ultraviolet absorber adheres to the roll group of the manufacturing apparatus during film formation, and may reattach to the film or be damaged. Since it becomes an optical fault, it is not preferable.

  Examples of inorganic ultraviolet absorbers include ultrafine particles of metal oxides such as cerium oxide, zinc oxide, and titanium oxide.

  The upper limit of the melting point is preferably higher from the viewpoint of heat resistance, but when the polyethylene terephthalate unit is the main component, the film having a melting point exceeding 250 ° C. tends to deteriorate moldability. In addition, transparency tends to deteriorate. Furthermore, in order to obtain high moldability and transparency, it is preferable to control the upper limit of the melting point to 245 ° C.

  Moreover, in order to improve handling properties, such as the slipperiness and winding property of a film, it is preferable to form an unevenness | corrugation on the film surface. As a method for forming irregularities on the film surface, a method of incorporating particles in the film is generally used.

  Examples of the particles include internal particles having an average particle size of 0.01 to 10 μm, external particles such as inorganic particles and / or organic particles. When particles having an average particle diameter exceeding 10 μm are used, defects in the film are liable to occur, and the design and transparency tend to deteriorate. On the other hand, in the case of particles having an average particle diameter of less than 0.01 μm, handling properties such as film slipperiness and winding property tend to be lowered. The lower limit of the average particle diameter of the particles is more preferably 0.10 μm, particularly preferably 0.50 μm, from the viewpoint of handling properties such as slipping property and winding property. On the other hand, the average particle diameter of the particles is more preferably 5 μm, particularly preferably 2 μm, from the viewpoint of transparency and reduction of film defects due to coarse protrusions.

  The average particle size of the particles is taken by taking a plurality of photographs of at least 200 particles by electron microscopy, tracing the outline of the particles on an OHP film, and converting the trace image to an equivalent circle diameter with an image analyzer. To calculate.

  Examples of the external particles include wet and dry silica, colloidal silica, aluminum silicate, titanium oxide, calcium carbonate, calcium phosphate, barium sulfate, alumina, mica, kaolin, clay, hydroxyapatite and the like, and styrene, silicone, acrylic Organic particles or the like containing acids as constituent components can be used. Among these, inorganic particles such as dry, wet and dry colloidal silica and alumina, and organic particles containing styrene, silicone, acrylic acid, methacrylic acid, polyester, divinylbenzene and the like as constituent components are preferably used. Two or more of these internal particles, inorganic particles and / or organic particles may be used in combination as long as the characteristics defined in the present invention are not impaired.

  Furthermore, the content of the particles in the film is preferably in the range of 0.001 to 10% by mass. When the amount is less than 0.001% by mass, the handling property is likely to be deteriorated, for example, the slipperiness of the film is deteriorated or winding becomes difficult. On the other hand, if it exceeds 10% by mass, it tends to cause formation of coarse protrusions, deterioration of film forming property and transparency.

Moreover, since the particle | grains contained in a film generally differ in refractive index from polyester, it becomes a factor which reduces the transparency of a film.
In many cases, the molded product is printed on the surface of the film before the film is molded in order to improve the design. Since such a printing layer is often applied to the back side of a molding film, it is desired that the transparency of the film is high from the viewpoint of printing clarity.

  Therefore, in order to obtain a high degree of transparency while maintaining the handleability of the film, the particles are not substantially contained in the base film of the main layer, and the particles are only in the surface layer having a thickness of 0.01 to 5 μm. It is effective to use a laminated film having a laminated structure containing. The upper limit of the thickness of the surface layer is preferably 3 μm, particularly preferably 1 μm. In this case, the particles exemplified above can be used.

  In the present invention, in order to adjust the haze of the film to 0.1 to 3.0%, the surface film having a thickness of 0.01 to 5 μm is formed without substantially including particles in the base film. Thus, a laminated structure in which particles are contained only in the surface layer is preferable. In addition, it is difficult to obtain a film having a haze of 2.0% or less only by incorporating particles in the film while maintaining handling properties.

Note that “substantially no particles are contained in the base film” as used above means, for example, in the case of inorganic particles, the content that is below the detection limit when inorganic elements are quantified by fluorescent X-ray analysis. means. This is because contaminants derived from foreign substances may be mixed without intentionally adding particles to the base film.
In order to obtain a film having a low haze and a high design property, it is preferable that the particles are not substantially contained in the base film, but particles may be added to the base film as long as they are 30 ppm or less.

  The thin surface layer can be formed by a coating method or a coextrusion method. Especially, in the case of the coating method, since the adhesiveness with a printing layer can also be improved by using the composition which consists of adhesiveness modification resin containing particle | grains as an application layer, it is a preferable method. As said adhesive property modification resin, resin which consists of at least 1 sort (s) chosen from polyester, a polyurethane, an acrylic polymer, and / or those copolymers is preferable.

  As the particles to be contained in the surface layer, the same particles as those described above can be used. Among the particles, silica particles, glass fillers, and silica-alumina composite oxide particles are particularly suitable from the viewpoint of transparency because the refractive index is relatively close to that of polyester.

  Furthermore, the particle content in the surface layer is preferably in the range of 0.01 to 25% by mass. When the content is less than 0.01% by mass, handling properties are likely to deteriorate, for example, the slipperiness of the film is deteriorated or winding becomes difficult. On the other hand, when it exceeds 25 mass%, transparency and applicability tend to deteriorate.

  In order to impart other functions, the polyester film of the present invention can be made into a laminated structure by a known method using different types of polyester. The form of the laminated film is not particularly limited. For example, the laminated film has an A / B two-kind two-layer structure, a B / A / B two-kind three-layer structure, and a C / A / B three-kind three-layer structure. The form is mentioned

  It is important that the molding polyester film of the present invention is a biaxially stretched film. In the present invention, due to molecular orientation by biaxial stretching, the thermal deformation rate of the film under micro tension (initial load 49 mN) can be controlled within the range of the present invention, which is a disadvantage of the unstretched sheet. Solvent resistance and dimensional stability are improved. That is, it is one of the features of the present invention that the solvent resistance and heat resistance, which are defects of the unstretched sheet, are improved while maintaining the good formability of the unstretched sheet.

Method for producing a biaxially oriented polyester film, dried as needed polyester resin is supplied to a known melt extruder, a casting drum from a slit-shaped die extrusion into a sheet, the method such as electrostatic application is brought into close contact, and cooled and solidified, after obtaining an unstretched sheet (raw), such unstretched sheet is a method of biaxial stretching.

  As the biaxial stretching method, a method is employed in which an unstretched sheet is stretched and heat-treated in the longitudinal direction (MD) and width direction (TD) of the film to obtain a biaxially stretched film having a desired in-plane orientation degree. . Among these methods, in terms of film quality, the MD / TD method in which the film is stretched in the longitudinal direction and then stretched in the width direction, or the TD / MD method in which the film is stretched in the width direction and then stretched in the longitudinal direction. An axial stretching method and a simultaneous biaxial stretching method in which the longitudinal direction and the width direction are stretched almost simultaneously are desirable. In the case of the simultaneous biaxial stretching method, a tenter driven by a linear motor may be used. Furthermore, if necessary, a multistage stretching method in which stretching in the same direction is performed in multiple stages may be used.

  The film stretching ratio when biaxially stretching is preferably 1.6 to 4.2 times in the longitudinal direction and the width direction, particularly preferably 1.7 to 4.0 times. In this case, the stretching ratio in the longitudinal direction and the width direction may be either larger or the same ratio. More preferably, the stretching ratio in the longitudinal direction is 2.8 to 4.0 times, and the stretching ratio in the width direction is 3.0 to 4.5 times.

  As the stretching conditions for producing the molding polyester film of the present invention, for example, the following conditions are preferably employed.

  In the longitudinal stretching, it is more preferable that the stretching temperature is 50 to 110 ° C. and the stretching ratio is 1.6 to 4.0 times so that the subsequent lateral stretching can be performed smoothly.

  Usually, when stretching the polyethylene terephthalate, if the stretching temperature is lower than the appropriate conditions, the yield stress increases rapidly at the beginning of the lateral stretching, and therefore stretching cannot be performed. Moreover, even if it can extend | stretch, since thickness and a draw ratio become easy to become nonuniform, it is unpreferable.

  In addition, when the stretching temperature is higher than appropriate conditions, the initial stress is low, but the stress does not increase even when the stretch ratio is high. Therefore, the film has a small stress at 100% elongation at 25 ° C. Therefore, by taking the optimum stretching temperature, a highly oriented film can be obtained while ensuring stretchability.

  However, when the copolymerized polyester contains 1 to 40 mol% of a copolymer component, the stretching stress rapidly decreases as the stretching temperature is increased so as to eliminate the yield stress. In particular, since the stress does not increase even in the latter half of the stretching, the orientation does not increase and the stress at 100% elongation at 25 ° C. decreases.

  Such a phenomenon is likely to occur when the thickness of the film is 60 to 500 μm, and is particularly noticeable in a film having a thickness of 100 to 300 μm. Therefore, in the case of a film using the copolymerized polyester of the present invention, the stretching temperature in the transverse direction is preferably set as follows.

First, preheating temperature is performed in the range of +10 degreeC-+50 degreeC of the glass transition temperature at the time of measuring the mixture (original fabric) after extruding a film material with an extruder in DSC. Next, in the first half of the transverse stretching, the stretching temperature is preferably −20 ° C. to + 15 ° C. with respect to the preheating temperature. In the latter half of the transverse stretching, the stretching temperature is preferably 0 ° C. to −30 ° C. with respect to the stretching temperature of the first half, and particularly preferably in the range of −10 ° C. to −20 ° C. with respect to the stretching temperature of the first half. It is. By adopting such conditions, the first half of the transverse stretching is easy to stretch because the yield stress is small, and the second half is easily oriented. In addition, it is preferable that the draw ratio of a horizontal direction shall be 2.5 to 5.0 times. As a result, it is possible to obtain a film that satisfies F100 ₂₅ and F100 ₁₀₀ defined in the present invention.

Furthermore, the film is subjected to heat treatment (heat setting treatment) after biaxial stretching. This heat treatment condition is an important condition for achieving both haze and surface roughness, that is, slipperiness of the film. The stretched film is subsequently heat-treated in the tenter. In this case, it is important to perform the heat treatment in two or more stages. The first stage heat treatment temperature (TS1) is in the range of −5 ° C. to −30 ° C. of the second stage heat treatment temperature (TS2), the lower limit is preferably TS2-10 ° C., and the upper limit is preferably TS2-25 ° C. is there. The second stage heat treatment temperature (TS2) is carried out in the range of −5 ° C. to −35 ° C. of the melting point when the mixture (raw material) after extruding the film material with an extruder is measured by DSC described later. The lower limit value of TS2 is preferably a melting point of −10 ° C., and the upper limit value of TS2 is preferably a melting point of −30 ° C. An intermediate heat treatment zone can be provided between TS1 and TS2, and a heat treatment zone can be provided after TS2. In these cases, TS2 shows the highest heat treatment temperature. By taking such conditions, a film having a low haze and good sliding properties can be obtained.
The heat treatment may be either a tension heat treatment or a relaxation heat treatment. In order to lower the heat shrinkage rate, a relaxation heat treatment of 3 to 10% is preferable.

  The reason is considered as follows. A polyester film containing about 5 to 50 mol% of a copolymer component as in the present invention has a lower crystallization speed and lower crystallinity than a polyethylene terephthalate film. Therefore, when heat treatment is performed rapidly at a high temperature after the end of stretching, the mobility of molecules constituting the material having low crystallinity is increased in the heat treatment zone. Therefore, the surface protrusion formed by the bulging of the particles (particles in the film and / or particles of the coating layer) in the stretching process is buried again in the heat treatment zone, so that sufficient surface roughness is obtained. I can't. Therefore, in order to wind up the film neatly, the content of the particles is increased beyond the necessary amount of the polyethylene terephthalate film, which causes haze deterioration. On the other hand, if the temperature of TS2 is lower than a predetermined temperature, a film having a sufficiently low thermal shrinkage at 150 ° C. cannot be obtained.

  Therefore, taking the method of the present invention in which the heat treatment zone has two stages (or more) is that the crystallization of the film is promoted to some extent before the particles are buried in the TS1 and the TS2 zone is sufficient. Even when the temperature is increased, the molecular mobility is sufficiently lowered as compared with the state of the previous paragraph, and the film is further promoted in crystallinity with the surface protrusions formed, and a film having a low thermal shrinkage rate can be obtained. Moreover, the addition of more than necessary particles can be prevented.

  In general, as a means for lowering the degree of plane orientation, a method of lowering the draw ratio and a method of increasing the blending amount of the copolymer component are known, but the former method deteriorates the thickness unevenness of the film. This is not preferable because the melting point is lowered and the heat resistance is deteriorated. In the present invention, in order to reduce the plane orientation degree of the biaxially oriented polyester film and the thermal shrinkage at 150 ° C., heat setting is performed at a higher temperature than usual. The heat setting is preferably performed in the above-described heat treatment, particularly the second heat treatment.

  Further, in the present invention, it is necessary to use a copolymer polyester as a biaxially oriented polyester film, and since the melting point is lower than that of a uniform polymer, if the heat setting temperature is increased, the clip that holds the film in the transverse stretching step is used. The film is fused and difficult to peel off. Therefore, it is important to sufficiently cool the vicinity of the clip when the clip releases the film at the tenter outlet. Specifically, in order to make it easy to peel the film and the clip, (1) a method of providing a heat shielding wall on the clip portion so that the clip is hardly heated, and (2) a method of adding a clip cooling mechanism to the tenter. (3) A method in which the cooling section after heat setting is set long in order to enhance the cooling capacity, and the entire film is sufficiently cooled. (4) The cooling efficiency is increased by increasing the length of the cooling section and the number of sections. It is preferable to employ a method of increasing the clip, and (5) a method of enhancing the cooling of the clip by using a type in which the return portion of the clip travels outside the furnace.

  As described above, by using the molding polyester film of the present invention, it is difficult to mold with the conventional biaxially oriented polyester film, and the vacuum at a molding pressure of 10 atm or less is low. Also in molding methods such as molding and pressure molding, it is possible to obtain a molded product with good finish. In addition, these molding methods are advantageous in terms of economy in the production of molded products because the molding costs are low. Therefore, application to these molding methods can most effectively exert the effect of the molding polyester film of the present invention.

  On the other hand, although the mold and the molding apparatus are expensive and disadvantageous in terms of economy, mold molding is characterized in that a molded product having a more complicated shape than that of the molding method is molded with high accuracy. Therefore, when the mold is molded using the molding polyester film of the present invention, molding is possible at a lower molding temperature and the finished quality of the molded product is improved as compared with the conventional biaxially oriented polyester film. The remarkable effect is expressed.

  Furthermore, the molded product thus molded has excellent elasticity and shape stability (heat shrinkage characteristics, thickness unevenness) when used in a normal temperature atmosphere, and also has excellent solvent resistance and heat resistance, and also has an environmental impact. Therefore, it can be suitably used as a molding member for home appliance nameplates, automobile nameplates, dummy cans, building materials, decorative plates, decorative steel plates, transfer sheets and the like.

  The molding polyester film of the present invention is also suitable as a molding material that is molded using a molding method such as press molding, laminate molding, in-mold molding, draw molding, or bending molding, in addition to the above-described molding methods. is there.

(Polyester film for molding with a hard coat layer)
Another embodiment of the present invention is a molding polyester film in which a hard coat layer is provided on at least one surface of the molding polyester film directly or via a surface layer made of an adhesion improving resin. In the present invention, the hard coat layer refers to a layer having a coating with a hardness higher than that of the base material in order to supplement the surface hardness of the base material made of the molding polyester film and improve the scratch resistance.

  The layer having a hard coat property that can be used in the present invention is not particularly limited, and a melamine-based, acrylic-based, silicon-based hard coat, etc. can be used. The hard coat layer is preferred.

  In a preferred embodiment of the acrylic hard coat layer in the present invention, a coating agent containing a polyfunctional (meth) acrylate compound having two or more (meth) acryloyl groups in one molecule is applied and then polymerized and / or reacted. Thus, a resin film is preferably used. One or more polyfunctional (meth) acrylate compounds may be used in combination.

Two or more (meth) acryloyl groups in one molecule in the present invention (however, the description of “(meth) acryloyl group” in the present invention is an abbreviation of acryloyl group or methacryloyl group). As the polyfunctional (meth) acrylate compound having, a compound in which the hydroxyl group of a polyhydric alcohol having two or more alcoholic hydroxyl groups in one molecule is an esterified product of two or more (meth) acrylic acids, etc. Can be used.
In particular, a coating containing a polyfunctional (meth) acrylate monomer compound having two (meth) acryloyl groups in one molecule and a monomer compound having three or more (meth) acryloyl groups in one molecule It is preferable to form a hard coat layer with an agent because of excellent scratch resistance and flexibility as well as hardness and curability.

  Specifically, as a polyfunctional (meth) acrylate compound having two (meth) acryloyl groups in one molecule, (a) (meth) acrylic acid diesters of alkylene glycol having 2 to 12 carbon atoms: ethylene glycol di (Meth) acrylate, propylene glycol di (meth) acrylate, 1,4-butanediol di (meth) acrylate, neopentyl glycol di (meth) acrylate, 1,6-hexanediol di (meth) acrylate, etc. (b) (Meth) acrylate diesters of polyoxyalkylene glycol: diethylene glycol di (meth) acrylate, triethylene glycol di (meth) acrylate, tetraethylene glycol di (meth) acrylate, dipropylene glycol di (meth) acrylate, polyester Renglycol di (meth) acrylate, polypropylene glycol di (meth) acrylate, etc. (c) Polyhydric alcohol (meth) acrylic acid diesters: pentaerythritol di (meth) acrylate, etc. (d) Bisphenol A or bisphenol A (Meth) acrylic acid diesters of hydride ethylene oxide and propylene oxide adducts: 2,2′-bis (4-acryloxyethoxyphenyl) propane, 2,2′-bis (4-acryloxypropoxyphenyl) propane, etc. , (E) a terminal isocyanate group-containing compound obtained by reacting a diisocyanate compound with two or more alcoholic hydroxyl group-containing compounds in advance, and further two in a molecule obtained by reacting an alcoholic hydroxyl group-containing (meth) acrylate. More than Urethane (meth) acrylates having a (meth) acryloyloxy group, (f) two or more (meta) in the molecule obtained by reacting a compound having two or more epoxy groups in the molecule with acrylic acid or methacrylic acid. ) Epoxy (meth) acrylates having an acryloyloxy group.

  Specific examples of the monomer compound having three or more (meth) acryloyl groups in one molecule include pentaerythritol tri (meth) acrylate, pentaerythritol tetra (meth) acrylate, and dipentaerythritol tri (meth). Examples include acrylate, dipentaerythritol tetra (meth) acrylate, dipentaerythritol penta (meth) acrylate, dipentaerythritol hexa (meth) acrylate, and trimethylolpropane tri (meth) acrylate. Moreover, the urethane acrylate compound which has 3 or more (meth) acryloyl groups in 1 molecule, and the epoxy acrylate compound which has 3 or more (meth) acryloyl groups in 1 molecule are mentioned.

  The proportion of the monomer having three or more (meth) acryloyl groups in one molecule is desirably 30 to 90% by mass with respect to the total solid content. When the proportion of the monomer used is less than 30% by mass, it is difficult to obtain a cured film having sufficient scratch resistance, and when the amount exceeds 90% by mass, the flexibility of the film decreases. In addition, cracks occur in the hard coat layer during molding, which is not preferable.

  Examples of a method of polymerizing and / or reacting the compound composition of the hard coat layer include a method of irradiating with an electron beam, radiation, or ultraviolet rays. When ultraviolet rays are irradiated, a photopolymerization initiator is added to the composition. Is desirable.

  Specific examples of the photopolymerization initiator include acetophenone, 2,2-diethoxyacetophenone, p-dimethylacetophenone, p-dimethylaminopropiophenone, benzophenone, 2-chlorobenzophenone, 4,4′-dichlorobenzophenone, 4,4′-bisdiethylaminobenzophenone, Michler's ketone, benzyl, benzoin, benzoin methyl ether, benzoin ethyl ether, benzoin isopropyl ether, methyl benzoyl formate, p-isopropyl-α-hydroxyisobutylphenone, α-hydroxyisobutylphenone, 2, Carbonyl compounds such as 2-dimethoxy-2-phenylacetophenone and 1-hydroxycyclohexyl phenyl ketone, tetramethylthiuram monosulfide, tetramethylthiu Examples thereof include sulfur compounds such as lamb disulfide, thioxanthone, 2-chlorothioxanthone, and 2-methylthioxanthone, and peroxide compounds such as benzoyl peroxide and di-t-butyl peroxide. Examples of these photopolymerization-initiated peroxide compounds such as t-butyl peroxide. These photopolymerization initiators may be used alone or in combination of two or more. The addition amount of the photopolymerization initiator is suitably 0.01 to 10% by mass in the solid content, and when the amount used is small, not only the reaction is slow and the productivity becomes poor, but also due to the remaining unreacted matter. Sufficient hard coat properties cannot be obtained. On the other hand, when the addition amount is large, there is a problem that the hard coat layer is yellowed by the photoinitiator.

  The compound composition forming the hard coat layer used in the present invention is known in the art such as hydroquinone, hydroquinone monomethyl ether, 2,5-t-butyl hydroquinone to prevent thermal polymerization during production and dark reaction during storage. It is desirable to add a thermal polymerization inhibitor. The addition amount of the thermal polymerization inhibitor is preferably 0.005 to 0.05% by mass in the solid content.

  For the purpose of improving the workability during coating and controlling the coating film thickness, an organic solvent is blended in the compound composition forming the hard coat layer used in the present invention within a range that does not impair the purpose of the present invention. be able to.

  As the organic solvent, those having a boiling point of 50 to 150 ° C. are preferable because it is necessary to adjust the drying temperature after coating to 150 ° C. or less from the problem of heat resistance of the molding polyester film as the base material. Specific examples include alcohol solvents such as methanol, ethanol and isopropyl alcohol, acetate solvents such as methyl acetate, ethyl acetate and butyl acetate, ketone solvents such as acetone and methyl ethyl ketone, and aromatic solvents such as toluene. And cyclic ether solvents such as dioxane. These solvents can be used alone or in admixture of two or more.

  Various additives can be blended in the hard coat layer of the present invention as required. For example, fillers for surface irregularities and relaxation of internal stress, fluorine and silicon compounds for imparting water repellency, leveling agents and antifoaming agents for improving coatability and appearance, and for coloring Dyes and pigments.

  The hard coat layer may be applied after the molding process, but is preferably laminated on a film before the molding process that can be continuously processed in a roll form. Examples of the lamination method include known methods, and specific examples include a spray method, a dipping method, a roll coating method, a die coating method, and a gravure coating method.

  The thickness of the hard coat layer is preferably 0.5 μm or more and 10 μm or less. When the thickness is thin, hard coat properties are difficult to obtain. Conversely, when the thickness is thick, curling due to curing shrinkage tends to be poor. A particularly preferred thickness is 1 μm or more and 6 μm or less.

  The film for molding provided with the hard coat layer of the present invention is capable of obtaining a molded product having good moldability and good finish, and can easily obtain a molded product having excellent surface scratch resistance. It can be suitably used as a molded member for automobile nameplates, dummy cans, building materials, decorative plates, decorative steel plates, and the like.

  Hereinafter, the present invention will be described in detail by way of examples. The film properties obtained in each example were measured and evaluated by the following methods.

(1) Intrinsic viscosity 0.1 g of a chip sample was precisely weighed, dissolved in 25 ml of a mixed solvent of phenol / tetrachloroethane = 60/40 (mass ratio), and measured at 30 ° C. using an Ostwald viscometer. In addition, the measurement was performed 3 times and the average value was calculated | required.

(2) Thickness unevenness A continuous tape-like sample of a film having a length of 3 m in the transverse stretching direction and a width of 5 cm in the longitudinal stretching direction is wound, and the thickness of the film is measured with a film thickness continuous measuring machine (manufactured by Anritsu Corporation). Record on the recorder. From the chart, the maximum value (Tmax), the minimum value (Tmin), and the average value (Tav) of the thickness were obtained, and the thickness unevenness (%) was calculated by the following formula. In addition, the measurement was performed 3 times and the average value was calculated | required. Moreover, when the length of a horizontal extending direction is less than 3 m, it joins and performs. In addition, the measurement data in the connection part was deleted.
Unevenness of thickness (%) = ((Tmax−Tmin) / Tav) × 100

(3) Haze Based on JIS-K7136-2000, the haze of the film was measured using a haze meter (Nippon Denshoku Industries Co., Ltd., 300A). In addition, the measurement was performed twice and the average value was calculated | required.

(4) Film thickness Using a millitron, 5 points per sheet, a total of 15 points were measured, and the average value was determined.

(5) Stress at 100% elongation, elongation at break With respect to the longitudinal direction and the width direction of the biaxially stretched film, a sample was cut into a strip shape having a length of 180 mm and a width of 10 mm, respectively, with a single-blade razor. Next, the strip-shaped sample was pulled using a tensile tester (manufactured by Toyo Seiki Co., Ltd.), and the 100% elongation stress (MPa) and elongation at break (%) in each direction were determined from the obtained load-strain curve. .

  The measurement was performed under the conditions of an initial length (distance between marked lines) of 40 mm, a distance between chucks of 100 mm, a crosshead speed of 100 mm / min, a chart speed of the recorder of 200 mm / min, and a load cell of 25 kgf in an atmosphere of 25 ° C. . In addition, this measurement was performed 10 times and the average value was used.

  In addition, a tensile test was performed under the same conditions as described above even in an atmosphere at 100 ° C. At this time, the sample was held for 30 seconds in an atmosphere at 100 ° C. and then measured. In addition, the measurement was performed 10 times and the average value was used.

(6) Surface roughness (Ra)
Based on JIS-B601-2001, Ra of the film was measured with Surfcom 304B (manufactured by Tokyo Seimitsu Co., Ltd.). The measurement conditions were a cutoff of 0.08 μm, a stylus radius of 2 μm, a measurement length of 0.8 mm, and a measurement speed of 0.03 mm / second.

(7) Thermal contraction rate at 150 ° C. A strip sample having a length of 150 mm and a width of 20 mm is cut out in the longitudinal direction and the width direction of the film, respectively. Two marks are made at 100 mm intervals in the length direction of each sample, and the distance A between the two marks is measured under no load. Subsequently, one side of each strip-shaped sample is hung with a clip on a basket under no load, and placed in a gear oven under an atmosphere of 150 ° C., and time is taken. After 30 minutes, the basket is removed from the gear oven and left at room temperature for 30 minutes. Next, the interval B is read for each sample under no load. From the read intervals A and B, the thermal shrinkage rate at 150 ° C. of each sample is calculated by the following formula: Thermal shrinkage rate (%) = ((A−B) / A) × 100

(8) Degree of plane orientation (ΔP)
Using a sodium D line (wavelength 589 nm) as a light source and using an Abbe refractometer, the refractive index (Nz) in the longitudinal direction of the film, the refractive index (Ny) in the width direction, and the refractive index (Nz) in the thickness direction are measured. The degree of plane orientation (ΔP) was calculated from the equation.
ΔP = ((Nx + Ny) / 2) −Nz

(9) Light transmittance at a wavelength of 370 nm The light transmittance of the film in the ultraviolet region of a wavelength of 370 nm was measured using a spectrophotometer (manufactured by Shimadzu Corporation, UV-1200).

(10) Rolling-out property of roll-shaped film The formed film is wound around a 3-inch paper tube having a width of 300 mm and a length of 200 m, and left for 72 hours in an atmosphere of 23 ° C. and 65 RH%. Then, when the film was installed in the vacuum evaporation machine and unwound at a speed of 50 m / min in an atmosphere of 1 × 10 ⁻⁴ torr, the following evaluation was made until the winding was completed. Judgment criteria were ◯ when there was no problem from all viewpoints, and x when there was at least one problem.
a. Film tear b. Occurrence of flapping c. Generation of loud sounds due to friction between films or between film / roll

(11) Glass transition temperature (Tg) and melting point (Tm) of raw material (object)
Using a differential scanning calorimeter (Mac Science, DSC3100S), about 7 mg of the raw material extruded under the conditions of each example was placed in a sample pan, the pan was capped, and the temperature was increased from room temperature to 300 ° C. in a nitrogen gas atmosphere. The temperature was measured at a temperature increase rate of 20 ° C./min. Tg (° C.) was determined based on JIS-K7121-1987, 9.3, and the melting point was determined by the melting peak temperature (Tpm) defined in 9.1.
The melting point of the biaxially oriented polyester film is also measured in the same manner to determine the melting peak temperature (Tpm).

(12) Light resistance In the dark box, the printed sample that was offset-printed at the position 3 cm directly below the fluorescent lamp (made by Matsushita Electric Co., Ltd., U-type fluorescent lamp FUL9EX) so that the printed surface of the printed sample is the back side Put it on. Next, light was continuously irradiated for 2000 hours, and the color difference (ΔE value) was measured according to JIS Z 8730 based on the color (a *, b *, L *) before and after the light irradiation on the printing surface side. . The smaller the color difference (ΔE value), the smaller the color change before and after the light irradiation, that is, the better the light resistance. The acceptable level of light resistance is 0.5 or less in color difference (ΔE value). The color difference (ΔE value) is calculated by the following formula.
ΔE = √ (Δa ² + Δb ² + ΔL ² )

(13) Formability (a) Vacuum formability After 5 mm square printing is performed on the film, the film is heated with an infrared heater heated to 500 ° C. for 10 to 15 seconds, and then at a mold temperature of 30 to 100 ° C. Vacuum forming was performed. In addition, the heating conditions selected the optimal conditions within the said range with respect to each film. The shape of the mold was a cup shape, the opening had a diameter of 50 mm, the bottom part had a diameter of 40 mm, the depth was 50 mm, and all corners were curved with a diameter of 0.5 mm. .

Five molded products that were vacuum-molded under the optimum conditions were evaluated for moldability and finish, and ranked according to the following criteria. In addition, (double-circle) and (circle) were set as the pass, and x was set as the disqualification.
◎: (i) There is no tear in the molded product,
(Ii) the corner radius of curvature is 1 mm or less, and the printing deviation is 0.1 mm or less,
(Iii) Further, there is no appearance defect corresponding to ×: (i) The molded product is not torn,
(ii) The corner radius of curvature is more than 1 mm and not more than 1.5 mm, or printing deviation is 0.1
greater than 0.2 mm and less than 0.2 mm,
(iii) Furthermore, there is no appearance defect corresponding to ×, and there is no problem in practical use. ×: The molded product is torn, or even if it is not torn, it falls under any of the following items (i) to (iv) What to do
(i) Corner radius of curvature exceeds 1.5mm
(ii) Large folds and poor appearance
(iii) The film is whitened and the transparency is lowered
(iv) Print misalignment exceeding 0.2 mm

(B) Compressive air moldability After 5 mm square printing is performed on the film, the film is heated for 10 to 15 seconds with an infrared heater heated to 500 ° C., and then subjected to 4 atm at a mold temperature of 30 to 100 ° C. Crushing was performed under pressure. In addition, the heating conditions selected the optimal conditions within the said range with respect to each film. The shape of the mold is a cup shape, the opening has a diameter of 60 mm, the bottom has a diameter of 55 mm, a depth of 50 mm, and all corners are curved with a diameter of 0.5 mm. .

The moldability and finish of five molded products that were pressure-molded under optimal conditions were evaluated and ranked according to the following criteria. In addition, (double-circle) and (circle) were set as the pass, and x was set as the disqualification.
◎: (i) There is no tear in the molded product,
(ii) The corner radius of curvature is 1 mm or less, and the printing deviation is 0.1 mm or less,
(iii) Further, there is no appearance defect corresponding to ×: (i) The molded product is not torn,
(ii) The corner radius of curvature is more than 1 mm and not more than 1.5 mm, or printing deviation is 0.1
greater than 0.2 mm and less than 0.2 mm,
(iii) Furthermore, there is no appearance defect corresponding to ×, and there is no problem in practical use. ×: The molded product is torn, or even if it is not torn, it falls under any of the following items (i) to (iv) What to do
(i) Corner radius of curvature exceeds 1.5mm
(ii) Large folds and poor appearance
(iii) The film is whitened and the transparency is lowered
(iv) Print misalignment exceeding 0.2 mm

(C) Mold formability After printing on the film, contact heating with a hot plate heated to 100 to 140 ° C for 4 seconds, followed by press molding at a mold temperature of 30 to 70 ° C and a holding time of 5 seconds. It was. In addition, the heating conditions selected the optimal conditions within the said range with respect to each film. The shape of the mold is a cup shape, the opening has a diameter of 50 mm, the bottom has a diameter of 40 mm, a depth of 30 mm, and all corners are curved with a diameter of 0.5 mm. .

The moldability and finish of the five molded products molded under optimal conditions were evaluated and ranked according to the following criteria. In addition, (double-circle) and (circle) were set as the pass, and x was set as the disqualification.
◎: (i) There is no tear in the molded product,
(ii) The corner radius of curvature is 1 mm or less, and the printing deviation is 0.1 mm or less,
(iii) Further, there is no appearance defect corresponding to ×: (i) The molded product is not torn,
(ii) The corner radius of curvature is more than 1 mm and not more than 1.5 mm, or printing deviation is 0.1
greater than 0.2 mm and less than 0.2 mm,
(iii) Furthermore, there is no appearance defect corresponding to ×, and there is no problem in practical use. ×: The molded product is torn, or even if it is not torn, it falls under any of the following items (i) to (iv) What to do
(i) Corner radius of curvature exceeds 1.5mm
(ii) Large folds and poor appearance
(iii) The film is whitened and the transparency is lowered
(iv) Print misalignment exceeding 0.2 mm

(14) Solvent resistance The sample was immersed in toluene adjusted to 25 ° C. for 30 minutes, and the appearance change before and after immersion was determined according to the following criteria. The haze value was measured by the method described above.
○: Little change in appearance, change in haze value is less than 1% ×: Change in appearance is observed, or change in haze value is 1% or more

(15) Print quality The film before printing was heat-treated at 90 ° C. for 30 minutes, and then four-color screen printing was performed.
Furthermore, the film provided with the printing layer was dried at 80 ° C. for 30 minutes. Evaluation of printing quality was made by visually judging the printing appearance such as the following clear feeling, printing suitability, printing misalignment and the like through the film from the back side, not from the printing side. The judgment criteria were ◯ when there was no problem from all viewpoints, △ when there was a problem at least at one point, and x when there was a problem at two or more points.
a. Clear feeling: The printed design is clear without being blocked by the base film or coating layer.
To look.
b. Printability: Color unevenness and missing due to poor transfer of printing ink c. Printing misalignment: The misalignment of printing cannot be determined visually.

(16) Scratch resistance According to JIS-K5600, the surface was reciprocated 20 times with # 0000 steel wool with a load of 1 kgf, and evaluated visually after being left for 24 hours.

Example 1
Copolymer polyester chip having an intrinsic viscosity of 0.69 dl / g, comprising 100 mol% of terephthalic acid units as aromatic dicarboxylic acid components, 40 mol% of ethylene glycol units and 60 mol% of neopentyl glycol units as diol components. (A), 0.04% by mass of amorphous silica having an intrinsic viscosity of 0.69 dl / g and an average particle diameter (SEM method) of 1.5 μm, and a benzotriazole-based ultraviolet absorber (N) (Ciba -The chip | tip (B) of the polyethylene terephthalate which contains 0.67 mass% of Specialty Chemicals Co., Ltd. and Tinuvin 326) was dried, respectively. Furthermore, the chip (A) and the chip (B) were mixed so as to have a mass ratio of 25:75. Subsequently, these chip mixtures were melt-extruded from the slit of the T die at 270 ° C. by an extruder and rapidly cooled and solidified on a chill roll having a surface temperature of 40 ° C. A stretched sheet was obtained.

  The obtained unstretched sheet was stretched 3.3 times at 90 ° C. in the longitudinal direction between the heating roll and the cooling roll. Next, the uniaxially stretched film was guided to a tenter, preheated at 120 ° C. for 10 seconds, and the first half of the transverse stretching was stretched 3.9 times at 110 ° C. and the latter half at 100 ° C. Furthermore, the first heat treatment (TS1) was 205 ° C., and the second heat treatment (TS2) was heat-set at 235 ° C. while performing a 7% relaxation treatment in the transverse direction, and a biaxially stretched polyester having a thickness of 100 μm. A film was obtained.

  In the heat setting zone, an intermediate section of 2 m is provided between the stretching section, a far infrared heater is installed in the heating section of the heat setting zone, and the limit position where the shielding plate in each section does not contact the film Expanded and installed. Also in the cooling section after heating, section shielding is strengthened, an external return method is used as a clip return method, a clip cooling device is installed, and forced cooling is performed with cold air of 20 ° C., and the clip temperature at the tenter outlet is set to 40. Measures were taken to prevent clip fusion to below ℃.

Comparative Example 1
In Example 1, a biaxially stretched polyester film was obtained in the same manner as in Example 1 except that the heat setting temperature was changed to 235 ° C. for both TS1 and TS2.

Comparative Example 2
In Example 1, a biaxially stretched polyester film was obtained in the same manner as in Example 1 except that the heat setting temperature was changed to 205 ° C. for both TS1 and TS2.

Example 2
In Example 1, a biaxially stretched polyester film was obtained in the same manner as in Example 1 except that the chip (B) was changed to a polyethylene terephthalate chip (C) containing no ultraviolet absorber.

Example 3
(Coating solution adjustment)
A water-soluble urethane resin (1st solid copolymer 3.15% by mass of copolymer polyester resin (Toyobo Co., Ltd., Vylonal MD-1250) and a terminal isocyanate group blocked with a hydrophilic group in a 40% by mass aqueous solution of isopropanol (first Elastolone H-3) manufactured by Kogyo Seiyaku Co., Ltd. in a solid content of 5.85% by mass, silica particles having an average particle size of 1.0 μm are 0.8% by mass based on the total resin, and silica having an average particle size of 0.05 μm. The coating solution was adjusted so that the particles contained 10% by mass with respect to the total resin. The obtained coating solution was adjusted to pH 6.5 using a 5% by mass aqueous sodium bicarbonate solution. Subsequently, it filtered with the bag type filter (Sumitomo 3M Co., Ltd. make, liquid filter bag), and stirred at 15 degreeC in the coating liquid circulation system stock tank for 2 hours.

The following chips (D), (J), and (F) were prepared as film raw materials of Example 3.
Chip (D) is a benzotriazole-based ultraviolet absorber comprising a resin component as an aromatic dicarboxylic acid component and a terephthalic acid unit of 100 mol%, a diol component as an ethylene glycol unit of 70 mol% and a neopentyl glycol unit of 30 mol%. This is a copolymer polyester chip containing 0.5% by mass of (N) (manufactured by Ciba Specialty Chemicals Co., Ltd., Tinuvin 326) and having an intrinsic viscosity of 0.77 dl / g.

The chip (J) is a polyethylene terephthalate chip containing 0.67% by mass of a benzotriazole ultraviolet absorber (N) (manufactured by Ciba Specialty Chemicals Co., Ltd., Tinuvin 326) and having an intrinsic viscosity of 0.77 dl / g. It is.
The chip (F) is a polypropylene terephthalate (PPT) containing 0.67% by mass of a benzotriazole ultraviolet absorber (N) (manufactured by Ciba Specialty Chemicals Co., Ltd., Tinuvin 326) and having an intrinsic viscosity of 0.75 dl / g. ) Chip.

  After each of the chips was dried, chip (D), chip (J), and chip (F) were mixed so that the mass ratio was 50:10:40. Subsequently, these chip mixtures were melt-extruded from the slit of the T die at 270 ° C. with an extruder, rapidly cooled and solidified on a chill roll having a surface temperature of 40 ° C., and at the same time, the amorphous mixture was adhered to the chill roll using an electrostatic application method. A stretched sheet was obtained.

  The obtained unstretched sheet was stretched 3.5 times at 83 ° C. in the longitudinal direction between the heating roll and the cooling roll. Next, the coating solution was applied to the chill roll surface side (F surface) of the uniaxially stretched film by a reverse kiss coating method so that the thickness of the resin solid before stretching was 0.9 μm. The laminated film having the coating layer was guided to a tenter while being dried, preheated at 95 ° C. for 10 seconds, and the first half of the transverse stretching was stretched 3.9 times at 80 ° C. and the latter half at 75 ° C. Furthermore, heat treatment was performed at 210 ° C. while the first heat treatment (TS1) was 190 ° C. and the second heat treatment (TS2) was subjected to a relaxation treatment of 7% in the transverse direction, and a biaxially stretched polyester having a thickness of 50 μm. A film was obtained.

  In the heat setting zone, an intermediate section of 2 m is provided between the stretching section, a far infrared heater is installed in the heating section of the heat setting zone, and the limit position where the shielding plate in each section does not contact the film Expanded and installed. Also in the cooling section after heating, section shielding is strengthened, an external return method is used as a clip return method, a clip cooling device is installed, and forced cooling is performed with cold air of 20 ° C., and the clip temperature at the tenter outlet is set to 40. Measures were taken to prevent clip fusion to below ℃.

Comparative Example 3
In Example 3, a biaxially stretched polyester film was obtained in the same manner as in Example 3 except that the heat setting temperature was changed to 205 ° C. for both TS1 and TS2.

Comparative Example 4
In Example 3, a biaxially stretched polyester film was obtained in the same manner as in Example 2 except that the heat setting temperature was changed to 180 ° C. (TS1) and 220 ° C. (TS2).

Example 4
The raw material composition of Example 3 is used as a core layer, and a chip in which chips (D) and chips (J) are mixed at a mass ratio of 50:50 is introduced into another extruder as a raw material for the skin layer, and melted at 280 ° C. In the same manner as in Example 2, except that the core layer raw material and skin layer / core layer / skin layer = 10/80/10 were joined by a feed block and then extruded from a T-die at 270 ° C. A biaxially stretched polyester film was obtained.

Reference Example 5
As raw materials of Reference Example 5, in addition to the above chip (J), the following chip (O) and chip (P) were prepared.
The chip (O) has an intrinsic viscosity of 0.71 dl / g, comprising 60 mol% of terephthalic acid units and 40 mol% of isophthalic acid units as aromatic dicarboxylic acid components and 100 mol% of ethylene glycol units as diol components. This is a copolyester chip.
The chip (P) has an intrinsic viscosity of 0.71 dl / unit, comprising 60 mol% of terephthalic acid units and 40 mol% of naphthalenedicarboxylic acid components as aromatic dicarboxylic acid components and 100 mol% of ethylene glycol units as diol components. g copolymerized polyester chip.

  The chip (J) and the copolymer polyester chip (O) and the polyethylene terephthalate chip (P) were mixed at a mass ratio of 50:25:25 and dried. Subsequently, these chip mixtures were melt-extruded from the slit of the T die at 270 ° C. with an extruder, rapidly cooled and solidified on a chill roll having a surface temperature of 40 ° C., and at the same time, the amorphous mixture was adhered to the chill roll using an electrostatic application method. A stretched sheet was obtained.

  The obtained unstretched sheet was stretched 3.5 times at 90 ° C. in the longitudinal direction between the heating roll and the cooling roll. Next, the uniaxially stretched film was guided to a tenter, preheated at 120 ° C. for 10 seconds, and the first half of the transverse stretching was stretched 3.9 times at 110 ° C. and the latter half at 100 ° C. Furthermore, the first heat treatment (TS1) was 205 ° C., and the second heat treatment (TS2) was heat-set at 238 ° C. while performing a 7% relaxation treatment in the transverse direction, and a biaxially stretched polyester having a thickness of 100 μm. A film was obtained.

  In the heat setting zone, an intermediate section of 2 m is provided between the stretching section, a far infrared heater is installed in the heating section of the heat setting zone, and the limit position where the shielding plate in each section does not contact the film Expanded and installed. Also in the cooling section after heating, section shielding is strengthened, an external return method is used as a clip return method, a clip cooling device is installed, and forced cooling is performed with cold air of 20 ° C., and the clip temperature at the tenter outlet is set to 40. Measures were taken to prevent clip fusion to below ℃.

Reference Example 6
Chip of copolymer polyester having an intrinsic viscosity of 0.69 dl / g, comprising 100 mol% of terephthalic acid unit as aromatic dicarboxylic acid component, 40 mol% of ethylene glycol unit and 60 mol% of neopentyl glycol unit as diol components A) and a polybutylene terephthalate chip (I) containing 0.04% by mass of amorphous silica having an intrinsic viscosity of 1.00 dl / g and an average particle diameter (SEM method) of 1.5 μm were dried. .
Next, chip (A), chip (I), benzotriazole-based ultraviolet absorber (N) (manufactured by Ciba Specialty Chemicals Co., Ltd., Tinuvin 326) was added at a mass ratio of 25.0: 74.5: 0.5 It mixed so that it might become. Next, these mixtures were melt-extruded from the slit of the T die at 265 ° C. by an extruder, rapidly cooled and solidified on a chill roll having a surface temperature of 20 ° C., and at the same time, the amorphous unstretched film was adhered to the chill roll using an electrostatic application method. A sheet was obtained.

  The obtained unstretched sheet was stretched 3.3 times at 80 ° C. in the longitudinal direction between the heating roll and the cooling roll. Next, the uniaxially stretched film was guided to a tenter, preheated at 95 ° C. for 10 seconds, and the first half of the transverse stretching was stretched 3.8 times at 85 ° C. and the latter half at 80 ° C. Furthermore, the first heat treatment (TS1) was 185 ° C. and the second heat treatment (TS2) was heat-set at 200 ° C. while performing a 7% relaxation treatment in the transverse direction, and a 100 μm thick biaxially stretched polyester. A film was obtained.

  In the heat setting zone, an intermediate section of 2 m is provided between the stretching section, a far infrared heater is installed in the heating section of the heat setting zone, and the limit position where the shielding plate in each section does not contact the film Expanded and installed. Also in the cooling section after heating, section shielding is strengthened, an external return method is used as a clip return method, a clip cooling device is installed, and forced cooling is performed with cold air of 20 ° C., and the clip temperature at the tenter outlet is set to 40. Measures were taken to prevent clip fusion to below ℃.

Regarding Examples 1 to 4, Reference Examples 5 and 6, and Comparative Examples 1 to 4, the raw material composition and polymer characteristics of the polymers used are shown in Table 1, and the production conditions and characteristics of the films are shown in Tables 2 to 5.

Example 7
On the polyester film for molding obtained in Example 3, the following hard coat coating solution was applied by a microgravure method so that the thickness after drying was 3 μm, dried with hot air at 80 ° C., and an output of 160 W / cm. A polyester film for molding having a hard coat layer was obtained by passing a position 20 cm under a high-pressure mercury lamp at a speed of 30 m / min. The moldability (vacuum moldability, pressure moldability, mold moldability) of the film provided with the hard coat layer was the same as that of the film of Example 3 in which the hard coat layer was not laminated. Moreover, the crack did not generate | occur | produce in the coating layer of the obtained molded article. In addition, as a result of evaluating the scratch resistance, the surface was good with no scratches. On the other hand, the scratch resistance of the molded product obtained by evaluation of the moldability (vacuum moldability, pressure moldability, mold moldability) of the molding film obtained in Example 3 without forming the hard coat layer was evaluated. Then, many scratches were generated and it was defective.
(Hard coat coating solution)
The following materials were mixed at a mass ratio shown below, stirred for 30 minutes or more, and then undissolved substances and foreign matters were removed using a filter having a nominal filtration accuracy of 1 μm to prepare a coating liquid A.
・ Methyl ethyl ketone 48.50 mass%
-Hexafunctional polyurethane-based acrylic monomer 35.00% by mass
(Arakawa Chemical Industries, beam set 575)
・ Bifunctional polyurethane acrylic monomer 15.00% by mass
(Arakawa Chemical Industries, beam set 505-A6)
-Photoinitiator 1.50% by mass
(Irgacure 184 made by Ciba Specialty)

  The molding polyester film of the present invention is excellent in moldability at the time of heat molding at a low temperature and a low pressure, so that it can be applied to a wide variety of molding methods, and when used in a normal temperature atmosphere as a molded product, It has excellent morphological stability (heat shrinkage characteristics, thickness unevenness), excellent solvent resistance and heat resistance, and has a small environmental impact. Further, when unwinding a long film wound up in a roll shape at the time of post-processing, blocking and tearing are unlikely to occur, resulting in excellent productivity. Furthermore, since it is highly excellent in smoothness and transparency, the printing quality improving layer of the film has various types such as letterpress printing, intaglio printing, planographic printing, screen printing, offset printing, gravure printing, inkjet printing, flexographic printing, etc. Designs such as printing layers, design layers, etc. are applied by decoration methods such as printing decoration, printing, transfer, painting, painting, vapor deposition, sputtering, CVD, laminating, etc., then mold molding, pressure molding, vacuum molding, etc. It is suitable for a three-dimensional decoration method that is molded by various molding methods, and has excellent in-mold moldability and emboss moldability. Therefore, it is suitable as a portable device such as a mobile phone, an audio, a portable player / recorder, an IC recorder, a car navigation system, a PDA or a casing or a member thereof such as a notebook PC, a nameplate member or a building material member of a household appliance or an automobile, The contribution to the world is great.

  In addition, by incorporating an ultraviolet absorber in the film and reducing the transmittance in the ultraviolet region, light resistance can be imparted, particularly for applications used outdoors (members for automobile exteriors or building materials). It is suitable as a molding material.

Claims (4)

A method for producing a molding polyester film satisfying the following requirements (1) to (6) comprising a biaxially oriented polyester film containing a copolymerized polyester:
In heat setting treatment after biaxial stretching,
The heat treatment is divided into two or more stages,
The first stage heat treatment temperature (TS1) is in the range of −5 ° C. to −30 ° C. of the second stage heat treatment temperature (TS2),
Second stage heat treatment temperature (TS2) is characterized in that in a range of -5 ° C. ~ - 35 ° C. of the melting point of the film, a manufacturing method of molding a polyester film.
(1) The copolymer polyester comprises (a) an aromatic dicarboxylic acid component, ethylene glycol, and a copolymer polyester composed of a glycol component containing a branched aliphatic glycol or alicyclic glycol as a copolymer component, or ( b) Consists of terephthalic acid and an aromatic dicarboxylic acid component containing isophthalic acid as a copolymer component, and a glycol component containing ethylene glycol. (2) The content of the copolymer component in the copolymer polyester is 5 to 50 mol. %,
(3) (a) The film contains particles, or (b) the film contains substantially no particles and contains particles only in the surface layer. (4) Longitudinal direction of the film at 150 ° C. And the heat shrinkage in the width direction is 0.01 to 5.0%
(5) Haze is 0.1 to 3.0%
(6) The surface roughness (Ra) of the film on at least one side is 0.005 to 0.030 μm.   The method for producing a molding polyester film according to claim 1, wherein the second stage heat treatment temperature (TS2) is the highest heat treatment temperature in the heat setting treatment. The method for producing a molding polyester film according to claim 1 or 2, wherein the molding polyester film further satisfies the following requirements (7) to (10).
(7) 100% elongation stress in the longitudinal and width directions of the film is 40 to 300 MPa at 25 ° C. and 1 to 100 MPa at 100 ° C.
(8) The branched aliphatic glycol is neopentyl glycol and 1,4-cyclohexanedimethanol which is the alicyclic glycol. (9) The melting point of the film is 200 to 245 ° C.
(10) Degree of plane orientation is 0.095 or less   The average particle diameter of the particles contained in the surface layer is 0.01 to 10 µm, and the particle content in the surface layer is 0.01 to 25% by mass. The manufacturing method of the polyester film for a shaping | molding of description.