JP5793390B2 - Biaxially oriented polyester film - Google Patents

Description

The present invention relates to a biaxially oriented polyester film arm, details, such as a lens sheet, a base film and used for the optical member such as a liquid crystal panel or a plasma display, such as a diffusion sheet or a hard coat film or the like, solar of the preferred biaxially oriented polyester film in the battery back surface protective film.

  As one of films for members often used for flat panel displays such as liquid crystal displays and plasma displays, there are polyester films represented by polyethylene terephthalate and polyethylene naphthalate.

  Moreover, these polyester films are often used as a back surface protective film for solar cells.

  Since these polyester films improve heat resistance, mechanical strength, solvent resistance, etc., in many cases, biaxially oriented films that are oriented and crystallized by biaxial stretching and heat setting are used. However, these biaxially oriented polyester films are oriented and crystallized, so that the film surface is also highly oriented and crystallized, resulting in a decrease in adhesion to various topcoats. For this reason, providing an anchor coat layer (easy adhesion layer) for improving adhesiveness is widely performed. This easy-adhesion layer is often used in the film-forming process, using a so-called in-line coating method in which an aqueous easy-adhesion layer is applied to the film and then stretched in at least one direction and heat-set. It is done.

  As a biaxially oriented polyester film having such an easy-adhesion layer, we have already proposed a film using a urethane resin having a polycarbonate structure for the easy-adhesion layer. (Cited document 1) This film is excellent in adhesiveness with a solvent-free UV curable resin used for a lens layer of a lens sheet.

  By the way, in recent years, televisions using flat panel displays such as liquid crystal displays and plasma displays, which have been spreading worldwide, have already surpassed the prevalence of televisions using cathode ray tube displays in Japan. It is also spreading to emerging and developing countries overseas. Along with this, the price of liquid crystal panels and plasma display panels has been reduced, and the members used therefor have the same tendency.

  Solar cell panels are also being put into practical use on a global scale, but it is said that the key to further spread is the price of the panel itself, and the price has been reduced. Yes.

  On the other hand, in recent years, recycling of materials has been promoted especially in the field of synthetic resins because of increasing concern about the global environment such as global warming due to CO2 emissions and fears of depletion of petroleum resources. Therefore, for films for optical members used in flat panel displays and solar cell back surface protection films, for example, recycling scrap generated during film production contributes to CO2 emission reduction and efficient use of petroleum resources. It is also suitable for economic rationality.

  When producing a polyester film with an easy-adhesion layer, for example, scrap that does not become a product such as a part that does not become a by-product when slitting to a predetermined width, or a film roll that breaks before reaching a predetermined length Always occurs. If these scraps can be reused as raw materials, as described above, the manufacturing cost will be reduced, and CO2 emissions will be reduced, and oil resources will be used efficiently.

  However, in many cases, when a scrap of a polyester film having an easy-adhesion layer is recycled, coloring such as yellowing of the film occurs due to the influence of the easy-adhesion layer. In particular, in the case of having an easy-adhesion layer using a urethane resin having excellent adhesiveness in a wide range of applications, the problem of coloring is often very significant. In particular, in the case of a film for an optical member, when the film is transparent and thick, the brightness of the film is lowered, and even a slight coloring of a single film becomes conspicuous, so that improvement is required.

JP 2009-220376 A

The present invention has been made in view of the above-mentioned circumstances, and the problem to be solved is the adhesiveness between the lens layer, the diffusion layer and the hard coat layer used in the liquid crystal panel, and the EVA sheet of the sealing material of the solar battery cell. In spite of being included as a regenerated raw material generated in the production process of the film, there is little coloration of the film and a decrease in luminance, and it is excellent as a film for the above-mentioned use. _2. To provide a film that contributes to the reduction of emissions, the efficient use of petroleum resources, and is also economically rational.

  As a result of intensive studies on the above problems, the present inventors have found that the above problems can be solved if the biaxially oriented polyester film satisfying specific conditions and the production method thereof are completed, and the present invention is completed. It came to do.

  That is, the gist of the present invention is that at least one side of a base polyester film has a coating layer by in-line coating containing a polyurethane having at least one of a polycarbonate skeleton or a polyether skeleton and a crosslinking agent, and the total nitrogen amount is 30 ppm. The present invention is a biaxially oriented polyester film characterized by containing 5% by weight or more of a self-regenerating raw material in a base polyester film.

  In the present invention, the polyester film includes, for example, a lens layer used in a liquid crystal panel, a diffusion layer, a hard coat layer, and an EVA (ethylene-vinyl acetate copolymer) sheet that is a sealing material for solar cells. In spite of having a coating layer with excellent adhesiveness and a polyester film having a coating layer generated in the film production process as a raw material, there is little coloration or reduction in luminance of the polyester film. Therefore, it is excellent as a lens sheet, a diffusion sheet, a base film for a hard coat film, and a film for protecting the back surface of a solar cell, and contributes to CO2 emission reduction, efficient use of petroleum resources, and is also economically rational. Is.

Hereinafter, the present invention will be described in detail.
The biaxially oriented polyester film in the present invention is composed of aromatic polyester such as polyethylene terephthalate and polyethylene-2,6-naphthalate as a constituent component of the polyester, and a copolymer mainly composed of constituent components of these resins. Things.

  When the polyester is a copolyester, it is preferably a copolymer having a third component content of 10 mol% or less. As the dicarboxylic acid component of the copolymer polyester, one or more selected from isophthalic acid, phthalic acid, terephthalic acid, 2,6-naphthalenedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, adipic acid, sebacic acid and the like Is mentioned. Examples of the glycol component include one or more selected from ethylene glycol, diethylene glycol, propylene glycol, butanediol, 1,4-cyclohexanedimethanol, neopentyl glycol, ethylene oxide adduct of bisphenol A, and the like. In addition, when the usage-amount of such a copolymerization component exceeds 10 mol%, the fall of the heat resistance of a film, mechanical strength, solvent resistance, etc. will become remarkable.

  Among the polyesters, those using polyethylene terephthalate as a constituent component and films using the copolymerized polyester are preferable in terms of the balance between the properties as a base film and the cost.

  The above polyester is obtained by a conventionally known method, for example, by directly reacting a dicarboxylic acid and a diol to obtain a low polymerization degree polyester, or by reacting a lower alkyl ester of a dicarboxylic acid and a diol with a conventionally known transesterification catalyst. Then, it can obtain by the method of superposing | polymerizing in presence of a polymerization catalyst. As the polymerization catalyst, a known catalyst such as an antimony compound, a germanium compound, a titanium compound, an aluminum compound, or an iron compound may be used. However, when the amount of the antimony compound is zero or 100 ppm or less as antimony, the film becomes dull. The method of reducing can also be used preferably. In addition, these polymerizations can be carried out in a molten state to a desired degree of polymerization, or solid phase polymerization can be used in combination.

  In particular, polyester raw materials used in combination with solid phase polymerization for the purpose of reducing the amount of oligomers contained in polyester as a supplementary raw material to supplement the decrease in the intrinsic viscosity of polyester due to the use of recycled raw materials It is preferable to use it.

  The intrinsic viscosity of the polyester used for the polyester film is preferably 0.40 to 0.90 dl / g, more preferably 0.45 to 0.85 dl / g. If the intrinsic viscosity is too low, the mechanical strength of the film tends to decrease. Moreover, when intrinsic viscosity is too high, the load in the melt extrusion process at the time of film formation will be large, and there exists a tendency for productivity to fall.

The biaxially oriented polyester film in the present invention may be a laminated film in which two or more layers of polyester are laminated by a coextrusion method. When the film has three or more layers, the film is composed of two outermost layers and an intermediate layer which may itself be a laminated structure. The thicknesses of the two outermost layers are each usually 2 μm or more. Preferably, the ratio is 5 μm or more, and on the other hand, the ratio is usually ¼ or less, preferably 1/10 or less of the total film thickness.
Moreover, the thickness of the film of both surface layers may be the same, and may differ.

  Furthermore, the oligomers contained in the polyester film are deposited on the surface of the film due to heat history during film processing, etc., so that it becomes a foreign substance and deteriorates the transparency of the film. It is possible to use polyester that has been removed.

As the low-oligomerized polyester, it is possible to use a polyester polymerized by using the above-described solid phase polymerization together, or a polyester using hot water treatment or steam treatment.
These polyesters can be used for the entire film when the film has a single layer structure, and when the film has a multi-layer structure, a low oligomerized polyester can be used only for both surface layers.

  In the biaxially oriented polyester film in the present invention, it is possible to increase transparency without intentionally adding a filler. In order to ensure slipperiness as a film and to prevent scratches during the process, inorganic fine particles And organic fine particles can be added to the film or deposited. The fine particles to be added to the polyester film are not particularly limited. For example, silicon oxide, calcium carbonate, magnesium carbonate, calcium phosphate, magnesium phosphate, kaolin, talc, alumina, titanium oxide, barium sulfate, etc. Inorganic fine particles, and crosslinked polymer particles such as crosslinked acrylic resin, crosslinked polystyrene resin, thermosetting urea resin, thermosetting phenol resin, thermosetting epoxy resin, and benzoguanamine resin can be used. Among these, in order to obtain a high degree of transparency, it is preferable to use amorphous silica particles having a refractive index relatively close to that of polyester and less void formation in the biaxially oriented polyester film.

When the film is white and needs to have a concealing property, white pigments such as titanium oxide, zinc oxide, zinc sulfide, and barium sulfate can be used.
Furthermore, when it is necessary that the film is black or colored other than white or black, a black pigment such as carbon black, or an inorganic or organic coloring pigment can be added.

  The fine particles and pigments having an average particle diameter in the range of usually 0.001 to 5 μm can be used alone or in combination of two or more. Moreover, it is preferable to select the addition amount from the range of 0.0005-25 weight% normally.

  In particular, when it is used for an optical film for a flat panel display member such as a prism sheet, since transparency is required, it is possible not to have fine particles in the polyester film, and the polyester film has three or more layers. As a laminated structure of the above, a method of ensuring slipperiness while maintaining the transparency of the polyester film by adding fine particles only to both surface layers without actively adding fine particles to the intermediate layer is also used. Can do. In particular, when the film thickness is large (for example, 100 μm or more) and the transparency of the film is required, it is effective to prevent the presence of fine particles or to add fine particles only to both surface layers. At this time, as a film for an optical member, the film haze is preferably 3.0% or less, and preferably 2.5% or less.

  Further, in the biaxially oriented polyester film of the present invention, additives such as conventionally known antioxidants, heat stabilizers, lubricants, fluorescent brighteners and the like may be added as necessary in addition to the above fine particles. Can do. These additives are preferable because the polyester film has a laminated structure of three or more layers, and is added to the intermediate layer in order to prevent the additive from being deposited on the film surface.

  The thickness of the biaxially oriented polyester film in the present invention is preferably 25 μm or more, and more preferably 50 μm or more, as the thickness at which the effects of the present invention are obtained. When thickness is less than 25 micrometers, it becomes difficult to exhibit the effect of the coloring reduction of a film. On the other hand, the upper limit of the thickness is not particularly limited, but is usually 500 μm or less, preferably 400 μm or less.

  In the present invention, at least one surface of the base polyester film is a coating layer (hereinafter, referred to as coating layer X) by in-line coating containing a polyurethane having at least one of a polycarbonate skeleton or a polyether skeleton and a crosslinking agent. The total nitrogen content is 30 ppm or less, and the base polyester film needs to contain 5% by weight or more of a self-regenerating raw material. This total nitrogen amount is preferably 25 ppm or less, more preferably 20 ppm or less. If the total nitrogen content is 30 ppm or less, even if this film is repeatedly used as a recycled material, the film is less colored.

  This total nitrogen amount can be measured using a nitrogen measuring device. The nitrogen measuring device thermally decomposes a film sample in the presence of a catalyst, converts nitrogen into nitric oxide, and reacts this nitric oxide gas with ozone, thereby quantifying nitrogen from the intensity of chemiluminescent light. Is.

  The lower limit of the total nitrogen amount is not particularly defined, but since the coating layer X containing the polyurethane is included, the total nitrogen amount is not 0 ppm. However, a nitrogen measuring device that measures the total amount of nitrogen may have a measurement lower limit value at which a reproducible measurement value is obtained, but may be equal to or lower than this measurement lower limit value.

  The total amount of nitrogen is such that when only the coating layer X is provided on one side, when the coating layer X is provided on both sides, the coating layer X is provided on one side, and the other side is other than the coating layer X. This includes the total amount of nitrogen of the polyester film itself and the coating layer as the base material, including the case where a coating layer (hereinafter referred to as coating layer Y) is provided by in-line coating.

  Originally, the polyester does not contain a nitrogen-containing component, but by using a recycled raw material derived from a polyester film having a coating layer containing nitrogen as a part of the raw material, the polyester film itself contains a nitrogen component. Become. And this nitrogen component becomes a factor which colors a polyester film. Therefore, in order to reduce the coloration of the polyester film, it is important to reduce the nitrogen component mixed in the polyester film. Examples of means for this purpose include the following.

1. 1. Reduce the nitrogen component in the coating layer. 2. Reduce the thickness of the coating layer. Reduce the proportion of materials used for recycling. Thicken the polyester film that is the base material Among these, the thickness of the polyester film that is the base material for 4 is already determined by the application, so it is generally less flexible . Therefore, by combining the means 1 to 3, the nitrogen component mixed in the polyester film is reduced, but the amount of nitrogen in the film is determined by the product of the effects of these means.

  On the other hand, reducing the nitrogen component in one coating layer and reducing the thickness of the second coating layer are factors that greatly affect the properties of the coating layer, particularly the adhesion. On the other hand, the ratio of the raw material used for recycling 3 can be increased by an amount corresponding to the amount of nitrogen reduced by means 1 and 2. Therefore, it is important how to reduce the adhesiveness of the coating layer when the nitrogen component in the coating layer is reduced or the thickness of the coating layer is reduced. The coating layer for this will be described next.

  On at least one side of the biaxially oriented polyester film in the present invention, for example, a lens layer used in a flat panel display, a diffusion layer or a hard coat layer, and EVA (ethylene-vinyl acetate copolymer) used as a sealing material for solar cells. In order to provide adhesion to a sheet or the like, it has a coating layer (coating layer X) by in-line coating containing a polyurethane having at least one of a polycarbonate skeleton or a polyether skeleton and a crosslinking agent. is necessary. Here, the polyurethane having a polycarbonate skeleton or a polyether skeleton is a polyurethane using a compound having a polycarbonate skeleton or a polyether skeleton as a polyol. In addition, you may have a polycarbonate frame | skeleton and a polyether frame | skeleton simultaneously.

  The polycarbonate polyol used for the polyurethane of the coating layer X can be obtained by, for example, reaction of diphenyl carbonate, dialkyl carbonate, ethylene carbonate, or phosgene with a diol. Examples of the diol include ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, , 6-hexanediol, 1,4-cyclohexanediol, 1,4-cyclohexanedimethanol, 1,7-heptanediol, 1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, neo Examples include pentyl glycol, 3-methyl-1,5-pentanediol, 3,3-dimethylolheptane, 3,4-dimethyl-1,6-hexamethylenediol. Among these, a polycarbonate polyol using 1,6-hexanediol is preferable because it is easily available industrially, is good in terms of improving adhesiveness, and has good hydrolysis resistance.

  The polycarbonate polyol has a polystyrene-equivalent number average molecular weight by gel permeation chromatography (GPC) and is preferably 300 to 5,000.

  Polyether polyols used for the polyurethane of the coating layer X include polyoxyethylene glycol (polyethylene glycol), polyoxypropylene glycol (polypropylene glycol), polyoxytetramethylene glycol (polytetramethylene ether glycol), copolymer polyether polyol ( And block copolymers such as polyoxyethylene glycol and polyoxypropylene glycol, and random copolymers). Among these, polyoxytetramethylene glycol is preferable in terms of improving adhesiveness, and is also preferable because of its good hydrolysis resistance.

  The polyether polyol has a number average molecular weight in terms of polyethylene glycol determined by gel permeation chromatography (GPC) and is preferably 300 to 5,000.

  Polyurethanes using the above-described polycarbonate polyols and polyether polyols have better adhesion and resistance to hydrolysis than polyurethanes using polyester polyols, which are other general-purpose polyols.

  Each of these polycarbonate polyols or polyether polyols may be used alone or in combination of two or more. Further, as described above, these polycarbonate polyols and polyether polyols can be used in combination.

  Examples of the polyisocyanate used in the polyurethane of the coating layer X include known polyisocyanates such as aliphatic, alicyclic, and aromatic. In particular, in the present invention, aliphatic polyisocyanate and alicyclic polyisocyanate are used. The use of isocyanate is preferable because the degree of coloring is small when the film including the coating layer is recycled and melt-molded, and the adhesiveness of the coating layer is excellent.

  Specific examples of the aliphatic polyisocyanate include tetramethylene diisocyanate, dodecamethylene diisocyanate, hexamethylene diisocyanate, 2,2,4-trimethylhexamethylene diisocyanate, and 2-methylpentane-1,5-diisocyanate. .

  Specific examples of the alicyclic polyisocyanate include, for example, isophorone diisocyanate, hydrogenated xylylene diisocyanate, hydrogenated diphenylmethane-4,4′-diisocyanate, hydrogenated biphenyl-4,4′-diisocyanate, 1,4-cyclohexane diisocyanate. , Hydrogenated tolylene diisocyanate, 1,3-bis (isocyanatemethyl) cyclohexane, 1,4-bis (isocyanatemethyl) cyclohexane, and the like.

  Specific examples of the aromatic polyisocyanate include, for example, tolylene diisocyanate, 2,2′-diphenylmethane diisocyanate, 2,4′-diphenylmethane diisocyanate, 4,4′-diphenylmethane diisocyanate, 4,4′-diphenyldimethylmethane diisocyanate, 4,4'-dibenzyl diisocyanate, 1,5-naphthalene diisocyanate, xylylene diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate and the like can be mentioned.

  These polyisocyanates may be used alone or in combination of two or more.

  In the present invention, in order to reduce the amount of nitrogen in the coating layer (coating layer X) and develop excellent adhesiveness, the amount of polyisocyanate that is the source of nitrogen atoms in the polyurethane, that is, urethane, is described above. The amount of bonds and urea bonds is important. For this reason, it is preferable to select the amount of polyisocyanate so that the bond concentration of urethane and urea in the above-mentioned polyurethane is 500 to 3500 (eq / ton), more preferably 700 to 3000 (eq / ton).

  Examples of chain extenders include polyalcohols such as ethylene glycol, propylene glycol, butanediol, diethylene glycol, neopentyl glycol, trimethylol propane, hydrazine, ethylenediamine, piperazine, diethylenetriamine, isophoronediamine, 4,4′-diamino. Examples thereof include polyamines such as diphenylmethane and 4,4′-diaminodicyclohexylmethane, and water.

  The polyurethane having at least one of a polycarbonate skeleton or a polyether skeleton used for the coating layer (coating layer X) of the present invention is dissolved or dispersed in water containing a water-soluble organic solvent in a proportion of preferably 50% by weight or less. Those that do are preferred. In order to dissolve or disperse polyurethane in water, there are a forced emulsification type using an emulsifier, a self-emulsification type in which a hydrophilic group is introduced into the polyurethane, and a water-soluble type. In particular, a self-emulsification type in which an ionic group is introduced into a polyurethane skeleton to form an ionomer is preferable because of excellent storage stability of the liquid and water resistance, transparency and adhesiveness of the resulting coating layer.

  In this case, examples of the ionic group to be introduced include a carboxylate group, a sulfonate group, a phosphate group, and a phosphonate group as an anionic group, and a quaternary ammonium group as a cationic group. . For example, carboxylic acid group as an anionic group is exemplified by dimethylolpropionic acid, dimethylolbutanoic acid, bis- (2-hydroxyethyl) propionic acid, bis- (2-hydroxyethyl) butanoic acid, trimellitic acid- Ammonium salts such as bis (ethylene glycol) ester, lower amine salts, and the like can be preferably used. Moreover, about the quaternary ammonium of a cationic group, quaternization products, such as N-alkyl dialkanolamines, such as N-methyldiethanolamine and N-ethyldiethanolamine, can be used preferably. Among these ionic groups, when it is a carboxylate group and the counter ion is an organic amine having a boiling point of 150 ° C. or lower such as ammonia or triethylamine, the reactivity with an oxazoline-based crosslinking agent described later Is particularly preferable because it is high and becomes a cross-linking point of the coating layer.

  As a method for introducing an ionic group into the polyurethane, various methods can be taken in each stage of the polymerization reaction. For example, at the time of prepolymer synthesis, a resin having an ionic group can be used as a copolymerization component, or a component having an ionic group can be used as one component such as a polyol or a chain extender.

  In addition to the polyurethane described above, the coating layer (coating layer X) of the present invention needs to be used in combination with a crosslinking agent in order to impart heat resistance, heat-resistant adhesiveness, moisture resistance, blocking resistance, etc. to the coating layer. is there. This cross-linking agent is preferably water-soluble or water-dispersible. Specifically, in addition to melamine compounds, benzoguanamine compounds, urea compounds, acrylamide compounds, which are methylolated and alkoxymethylolated, epoxy compounds , An isocyanate compound, a carbodiimide compound, an oxazoline compound, a silane coupling agent compound, a titanium coupling agent compound, and the like can be selected. Among these cross-linking agents, when the cross-linking agent is water-soluble, it is preferable because the cross-linking reaction proceeds smoothly. It is particularly preferable for improving the adhesion of the layer. Such an oxazoline-based crosslinking agent is industrially available, for example, under the trade name Epocross (registered trademark) manufactured by Nippon Shokubai Co., Ltd. Moreover, the addition amount of these crosslinking agents is a weight ratio with respect to the polyurethane in the coating layer (polyurethane: crosslinking agent), and is used in a ratio of 95: 5 to 10:90, and further 90:10 to 20:80. Is preferred.

  In the coating layer (coating layer X) of the present invention, the total of the polyurethane and the crosslinking agent component described above is preferably present in an amount of 60% by weight or more, and more preferably 80% by weight or more. In addition to these resin components, other resins can be additionally added. Examples of the resin component that can be additionally added include polyester resins, acrylic resins, polyvinyl resins, and their graft polymers and polyester polyurethanes.

  In the present invention, it is also possible to add fine particles to the coating layer in order to prevent blocking of the coating layer X and to impart slipperiness. As fine particles, for example, inorganic particles such as silica, alumina, and metal oxide, and organic particles such as crosslinked polymer particles can be used. The size of the fine particles is 150 nm or less, preferably 100 nm or less, and the addition amount in the coating layer is preferably selected in the range of 0.5 to 10% by weight.

In addition, components other than those described above can be added to the coating layer X as necessary.
For example, surfactants, antifoaming agents, coatability improvers, thickeners, antioxidants, antistatic agents, ultraviolet absorbers and the like. These additives may be used alone or in combination of two or more.

  The coating layer (coating layer X) in the present invention is formed by using a so-called in-line coating method in which, as a coating solution mainly using water as a medium, it is stretched in at least one direction after being coated on a polyester film and further heat-set. However, the coating liquid used at this time is a ratio of 50% by weight or less, in addition to water, for the purpose of improving the dispersibility and storage stability, and improving the coating properties and coating film properties. It is possible to add one or more organic solvents compatible with water.

  Any known method can be applied as a method of applying the coating solution to the polyester film as the substrate. Specifically, roll coating method, gravure coating method, micro gravure coating method, reverse coating method, bar coating method, roll brush method, spray coating method, air knife coating method, curtain coating method, die coating method, etc. alone or in combination Can be applied.

The coating amount of the coating layer X described above can be selected from the range of 0.003 to 0.15 g / m ² as the final dry film after biaxial stretching, heat setting, and the like. When the coating layer thickness is less than 0.003 g / m ² , the adhesion may be insufficient. When the coating layer thickness exceeds 0.15 g / m ² , the adhesion is no longer saturated, and the total nitrogen amount is 30 ppm. In many cases, when the film having this coating layer is recycled, there is a concern that the coloring of the film becomes remarkable. The coating layer X described above is excellent in adhesiveness and can often reduce the coating amount. Specifically, even if the coating amount is in the range of 0.005 to 0.05, and further 0.005 to 0.03 g / m ² , it often has sufficient adhesiveness. By selecting such a coating layer composition, the total nitrogen amount can be reduced to 30 ppm or less.

  When the coating layer X containing the polyurethane having at least one of the above-described polycarbonate skeleton or polyether skeleton and the crosslinking agent is provided on both sides, or provided only on one side and there is no coating layer on the opposite side In addition, a coating layer may be provided on one side, and another coating layer (coating layer Y) may be provided on the opposite surface.

  The coating layer Y is provided in the film formation process by an in-line coating method, and is particularly limited if the total nitrogen amount of the polyester film including the coating layer X and the coating layer Y is 30 ppm or less. Although not intended, for example, for the purpose of imparting easy adhesion, slipperiness and antistatic properties, resin binders such as polyester resins, acrylic resins, polyvinyl resins, polyester polyurethanes, crosslinking agents, inorganic and Examples include organic fine particles, antistatic agents, surfactants and the like.

  By the way, when producing a polyester film having the above-mentioned coating layer, for example, a part that does not become a by-product when slitting to a predetermined width, or a product such as a film roll that is broken before reaching a predetermined length As described above, scrap that must not be generated is generated.

  In the present invention, it is necessary to contain 5% by weight or more of a recycled material derived from a polyester film having the above-mentioned coating layer (coating layer X) (referred to as a self-recycled material) as a base film material. Is 10% by weight or more. By doing so, it contributes to the reduction of CO2 emissions and the efficient use of petroleum resources, as well as to economic rationality. If more recycled materials are used, the contribution to them and the economic rationality become higher, so the upper limit is not particularly defined. However, if a large amount of recycled material is used, the total amount of nitrogen in the film including the coating layer will increase, resulting in significant coloration of the film and a tendency to cause adverse effects such as a decrease in the intrinsic viscosity of the film. Considering the generation rate of the scrap film to be used, 60% by weight is a standard.

  The above-mentioned self-regenerating raw material is mechanically cut and pulverized from the film state to form flakes. The flakes are once melt-extruded to form chips (pellets), or used as regenerated raw materials as they are. At this time, since the film having the coating layer X is melted and chipped (pelletized), the self-regenerating raw material receives a thermal history, and thus directly regenerated as flakes without chipping (pelletizing). It is preferable to use it as a raw material, and the ratio thereof is 50% by weight or more of the self-regenerating raw material, and it is preferable that all of the self-regenerating raw material is used as flakes. In that case, it is preferable to use a vent type twin screw extruder as an extruder for producing a polyester film. If a vent type twin-screw extruder is used, even if flakes are directly used as a raw material, it is possible to smoothly perform melt extrusion without causing a material biting failure during extrusion. Furthermore, the flakes are put into an extruder without drying, and when the polyester is in a semi-molten to molten state, a reduced pressure of 40 hectopascals or less, preferably 30 hectopascals or less, more preferably 20 hectopascals or less, is passed through the vent port. It can be maintained and degassed to remove moisture. By doing so, it is preferable because the heat drying step can be omitted and the heat history applied to the self-regenerating raw material can be reduced.

  The above self-regenerating raw material is used for the entire base film when the base polyester film has a single layer configuration, but when the base film has a laminated configuration, Self-regenerating raw materials may be used evenly in the layers, but when blended only in thicker layers or in higher concentrations in the laminated structure, when more self-regenerating raw materials are blended It is preferable in that the adverse effect can be further reduced. For example, when the laminated structure is a two-layer structure, it is preferable to blend only in a thicker layer or a higher concentration. When the laminated structure is three or more layers, as described above, the film is constituted by two outermost layers and an intermediate layer which may itself be a laminated structure, but the intermediate layer is set to be the thickest layer. Thus, it is preferable that the self-regenerating raw material is blended only in the intermediate layer or blended at a higher concentration.

  The biaxially oriented polyester film of the present invention, as a film including a coating layer, has a y value of 0.3240 or less, preferably 0.3235 when the color tone is measured by the reflection method of the spectroscopic colorimeter. In particular, when used as a film for an optical member, it is preferably 0.3230 or less. When the y value exceeds 0.3240, the film feels yellowish and the brightness is lowered.

  Hereinafter, although the manufacturing method of the biaxially-oriented polyester film of this invention is demonstrated concretely, as long as the summary of this invention is satisfied, this invention is not specifically limited to the following illustrations.

When the polyester film has a single layer configuration, one melt extruder is used, and when the polyester film has a multilayer configuration, a plurality of melt extruders required according to the stack configuration, and the combined lamination Feed block or multilayer multi-manifold die.
Supply dried self-regenerating raw materials and virgin polyester chips to a single-screw extruder by a known method, or supply undried self-regenerating raw materials and virgin polyester chips to a twin-screw extruder having a vent port connected to a vacuum system. Then, it is melted by heating to a temperature that is equal to or higher than the melting point of each polymer. At this time, it is preferable to use a known appropriate polymer filter for removing foreign substances. It is also possible to reduce the pulsation of the molten polymer using a gear pump as a preferable method. The molten polymer is then extruded from the die and rapidly solidified on a rotating cooling drum to obtain a substantially amorphous unoriented sheet. In this case, in order to improve the flatness of the sheet, it is preferable to improve the adhesion between the sheet and the rotary cooling drum. In the present invention, the electrostatic application adhesion method and / or the liquid application adhesion method are preferably employed.

  In the present invention, the unstretched sheet thus obtained is stretched in the biaxial direction to form a film. Specifically describing stretching conditions, when using the sequential biaxial stretching method, the unstretched sheet is preferably stretched 2 to 6 times in the machine direction (machine direction, MD direction) at 70 to 145 ° C, A longitudinally uniaxially stretched film is used. Next, after applying and drying the above-mentioned coating layer by an in-line coating method, the coating layer is stretched 2 to 6 times at 90 to 160 ° C. in the transverse direction (direction perpendicular to the machine direction, TD direction), and 160 to 245. Heat treatment is performed at a temperature of 1 to 600 seconds. In the case of using a simultaneous biaxial stretching machine, first, the above-mentioned coating layer is applied to the unstretched sheet by an in-line coating method and dried, and then the area magnification is 5 to 20 at 70 to 160 ° C. in the longitudinal and lateral directions. A method of performing heat treatment under the same conditions as the sequential biaxial stretching method after simultaneously stretching in the double range can also be used.

  Furthermore, there is also a method of relaxing 0.1 to 20% in the longitudinal direction and / or the transverse direction in the maximum temperature zone of heat treatment and / or the cooling zone at the heat treatment outlet, common to the sequential biaxial stretching method and the simultaneous biaxial stretching method. It can also be preferably employed. Further, it is possible to add re-longitudinal stretching and re-lateral stretching as necessary.

The biaxially oriented polyester film of the present invention can be produced at a low cost including a regenerated raw material, but can maintain a high luminance with little yellowing of the film. Moreover, since it has a coating layer (coating layer X), for example, a lens layer used in a liquid crystal panel, a solvent-based or solvent-free actinic radiation curable resin layer used for a diffusion layer, a hard coat layer, etc. It is suitable for a film for optical members because of its excellent adhesiveness with inorganic transparent conductive layers.
Moreover, since it is excellent also in adhesiveness with the EVA (ethylene-vinyl acetate copolymer) sheet | seat which is a sealing material for photovoltaic cells, a PVB (polyvinyl butyral) sheet | seat, etc., the film for back surface protection for solar cells It is also suitable for films for laminated glass.

  EXAMPLES Hereinafter, although an Example and a comparative example demonstrate this invention further more concretely, this invention is not limited to the following examples, unless the meaning is exceeded. In addition, the measurement and evaluation method of various physical properties of a film are shown below.

(1) Measurement of Intrinsic Viscosity of Polyester 1 g of polyester was accurately weighed and dissolved by adding 100 ml of a mixed solvent of phenol / tetrachloroethane = 50/50 (weight ratio), and measured at 30 ° C.

(2) Measurement of average particle diameter (d ₅₀ : μm) 50% of integration (weight basis) in equivalent spherical distribution measured using centrifugal sedimentation type particle size distribution measuring device “SA-CP3 type” (manufactured by Shimadzu Corporation) The value was defined as the average particle size.

(3) Film haze Film haze was measured with an integrating sphere turbidimeter “NDH2000” (manufactured by Nippon Denshoku Industries Co., Ltd.) according to JIS-K-7136.

(4) Total nitrogen analysis Analyzing the entire film including the coating layer using a solid state autosample changer ASC-120S (manufactured by Mitsubishi Chemical Analytech) connected to a nitrogen measuring device "TN-110 type" The amount of nitrogen was analyzed. For the calibration of the nitrogen amount, a mixture of dimethyl terephthalate and 1,5-diaminonaphthalene is used, and a master curve of the generated amount for the detection count of the N amount is created and stored. Combustion conditions are as follows: Combustion at a furnace temperature of 800 ° C (INLET 800 ° C, CATALYST 900 ° C). From the detection chart of N, it was confirmed that all contained nitrogen was detected within the program time, and this count was integrated. To do. From this integrated count, the amount of nitrogen was determined by a master curve and divided by the sample weight to obtain the total nitrogen content (weight ppm). Nitrogen detection sensitivity is measured by appropriately selecting Ultra (low concentration measurement, 1.25 to 10 ppm), High (medium concentration measurement, 2.5 to 75 ppm), and Middle (high concentration measurement, 5 to 200 ppm) for each sample. Then, an average value measured at 10 points was used as a measured value.

(5) Color tone reflection method y value of film The color tone reflection method y value of the film was measured with a spectrocolorimeter “CM-3730d” (manufactured by Konica Minolta). At this time, a C light source was set as the light source. In the measurement, for example, when the film thickness is 100 μm, 10 sheets are stacked, when 125 μm is stacked, 8 sheets are stacked, when 188 μm is stacked, 5 sheets are stacked, and when 250 μm is stacked, four sheets are stacked, so that the total thickness is 900 μm to 1000 μm. A plurality of sheets were overlapped for measurement.

(6) Moisture- and heat-resistant adhesion to the prism layer On the surface of the coating layer (coating layer X) of the prepared biaxially oriented polyester film, a composition for forming the prism layer shown below is used as a coating solution, and 50 g / It was coated in a thickness of m ^2. After that, the prism layer is molded by pressure bonding to a prism layer molding die roll formed with a reverse shape of a prism type lens (0.05 mm pitch), and at the same time from the opposite side of the prism layer (film substrate side) Ultraviolet irradiation was performed under the conditions of: That is, using a high-pressure mercury lamp having an energy of 160 W / cm, irradiation was performed for 30 seconds at an irradiation distance of 150 mm to cure the prism layer.

<Composition of prism layer forming coating solution>
1,9-nonanediol diacrylate 80 parts Ethylene oxide modified bisphenol A dimethacrylate 20 parts UV reaction initiator 4 parts (IRGACURE 184 manufactured by Ciba Specialty Chemicals)
The film formed by laminating the prism layer prepared above was treated at 80 ° C. and 85% RH for 50 hours, and then subjected to humidity control at 23 ° C. and 50% RH for 24 hours.

A cross-cut (25 squares of 2 mm ² ) reaching the base film is applied to the prism layer, and 18 mm tape (Cello Tape (registered trademark) CT-18 manufactured by Nichiban Co., Ltd.) is pasted thereon. After peeling off rapidly at a peeling angle of 180 degrees, the peeled surface is observed, the number of peeled pieces (out of 25 pieces) is counted, and classified into the following reference rank. (○ is the practical limit)
A: No. of peeled pieces (out of 25 pieces)
○: The number of peeled pieces is 1 or more and less than 5 (in 25 pieces)
Δ: Peeling area is 5 or more and less than 10 (out of 25)
X: 10 or more peeled areas (out of 25)

(8) Moist heat resistant adhesion with EVA Two pieces of a biaxially oriented polyester film having a length of 300 mm and a width of 25 mm were cut out so that the longitudinal direction was the MD direction. On the other hand, one piece of the EVA film having a length of 50 mm and a width of 25 mm was cut out and overlapped so that the EVA film was sandwiched between the two polyester film pieces on the coating layer (coating layer X) surface. This was laminated using a heat seal device (TP-701-B manufactured by Tester Sangyo Co., Ltd.). The EVA film used was 486.00FC (fast-curing type, thickness 0.5 mm) manufactured by Etimax Solar, Germany, and the heat seal conditions were a temperature of 150 ° C. and a pressure of 0.13 MPa for 20 minutes. The laminate film was treated at 80 ° C. and 85% RH for 500 hours, and then subjected to temperature control and humidity control at 23 ° C. and 50% RH for 24 hours.

  In order to measure the adhesive strength with EVA, first, a sample having a length of 300 mm and a width of 15 mm is cut out from a polyester film / EVA film laminate piece having a width of 25 mm. The unlaminated end of this 15 mm wide polyester film piece is mounted in a tensile / bending tester (EZGraph manufactured by Shimadzu Corporation). Subsequently, the force (adhesive strength) required to separate the polyester film / EVA film laminate at an angle of 180 ° and a speed of 100 mm / min was measured for 10 samples, and the average values were classified as follows. did.

◎: Adhesive strength is 50 N / 15 mm width or more ○: Adhesive strength is 30 N / 15 mm width to less than 50 N / 15 mm width Δ: Adhesive strength is 10 N / 15 mm width to less than 30 N / 15 mm width ×: Adhesive strength is less than 10 N / 15 mm width

Examples and Comparative Examples are shown below, and the method for producing the polyester used in the Examples and Comparative Examples is as follows.
<Manufacture of polyester>
<Method for producing polyester (a)>
Using 100 parts by weight of dimethyl terephthalate and 60 parts by weight of ethylene glycol as starting materials, 0.09 parts by weight of magnesium acetate tetrahydrate as a catalyst is placed in the reactor, the reaction start temperature is set to 150 ° C., and the methanol is distilled off gradually. The reaction temperature was raised to 230 ° C. after 3 hours. After 4 hours, the transesterification reaction was substantially terminated. After 0.04 part of ethyl acid phosphate was added to this reaction mixture, 0.03 part of antimony trioxide was added and a polycondensation reaction was carried out for 4 hours. That is, the temperature was gradually raised from 230 ° C. to 280 ° C. On the other hand, the pressure was gradually reduced from normal pressure, and finally 0.3 mmHg. After the start of the reaction, the reaction was stopped at a time corresponding to an intrinsic viscosity of 0.68 due to a change in stirring power of the reaction vessel, and the polymer was discharged under nitrogen pressure. The intrinsic viscosity of the obtained polyester (a) was 0.68.

<Method for producing polyester (b)>
In the method for producing polyester (a), after adding 0.04 part of ethyl acid phosphate, 0.3 part of silica particles having an average particle diameter of 2.1 μm dispersed in ethylene glycol and 0.03 part of antimony trioxide were added. In addition, polyester (B) was obtained using the same method as the production method of polyester (A) except that the polycondensation reaction was stopped at the time corresponding to the intrinsic viscosity of 0.66. The obtained polyester (B) had an intrinsic viscosity of 0.66.

<Method for producing polyester (c)>
In the method for producing polyester (a), polyester (c) was obtained using the same method as the method for producing polyester (a) except that germanium oxide in an ethylene glycol solution was used as the polymerization catalyst. In addition, the addition amount of germanium oxide was added so that it might become 100 ppm in polyester as a germanium metal. The intrinsic viscosity of the obtained polyester (c) was 0.68.

<Method for producing polyester (d)>
Polyester (c) was used as a starting material, and solid phase polymerization was performed at 220 ° C. under vacuum to obtain polyester (d). The intrinsic viscosity of the polyester (d) was 0.75.

Examples 1-5, Comparative Examples 1-4:
Using the above-mentioned polyesters (d) and (b) mixed at a ratio of 88% by weight and 12% by weight, respectively, as a raw material for the A layer, using 100% by weight of the polyester (c) as a raw material for the B layer, Each is supplied to two vent type twin screw extruders and melted at 285 ° C., each of two types and three layers (A / B / A) having A layer as the outermost layer (surface layer) and B layer as an intermediate layer Melt extrusion was performed by laminating and joining with a multi-manifold die so as to have a layer structure. This was cooled and solidified on a cooling roll whose surface temperature was set to 40 ° C. using an electrostatic application adhesion method, to obtain an unstretched sheet. At this time, the discharge amounts of the two extruders were adjusted so that the A / B / A thickness component ratio was 4/92/4. In each melt line, foreign matter was filtered using a stainless sintered filter medium having a filtration particle size (initial filtration efficiency of 95%) of 15 μm, and a gear pump was installed to reduce pulsation of the melt polymer. Next, the film is stretched 3.2 times in the machine direction at a film temperature of 100 ° C. using the roll peripheral speed difference, and then the coating agent having the composition shown in Table 1 is used as the coating layer X or coating layer Y as shown in Table 2 After coating on one or both sides of the film by a bar coating method, the film was guided to a tenter and stretched 4.0 times at 130 ° C. in the transverse direction, heat fixed at 227 ° C., and then in the cooling zone at the heat fixing outlet. The biaxially oriented polyester film having a thickness of 188 μm was relaxed by 5% in the transverse direction. The film was slit at both ends to form a film roll having a width of 1000 mm and a length of 1000 m. In addition, the coating thickness in following Table 2 and 3 is the thickness of the coating layer in the last film.

  Next, the scrap film at the end having the coating layer on one side or both sides generated when the film was slit was mechanically cut and pulverized and stored as flakes in a flake tank. When the flakes accumulated to some extent, the recycled flakes were added as they were to the intermediate layer (B layer) without heating and drying. At this time, the addition amount was 30% by weight with respect to the whole film, and the polyester (c), which is the virgin raw material for the B layer, was reduced and added accordingly. Others are performed in exactly the same manner as in the above-described film formation to prepare a biaxially oriented polyester film having a thickness of 188 μm. The film is slit at both ends to form a 1000 mm wide and 1000 m long film roll, and both ends of the film are slit. The scrap film generated at that time was similarly used as the flakes as the B layer raw material. Thus, the recycling of the scrap film was repeated, and the film rolls when the virgin resin was recycled three times at first were used as the films of Examples 1 to 5 and Comparative Examples 1 to 4, respectively.

Polycarbonate polyurethane: (u1)
Aqueous dispersion of polycarbonate polyurethane composed of hydrogenated diphenylmethane diisocyanate, poly (1,6-hexanediol carbonate) having a number average molecular weight of 2000, dimethylolbutanoic acid neutralized with triethylamine, and bond concentration of urethane and urea Is 1170 eq / ton.
Polycarbonate polyether polyurethane: (u2)
It is composed of isophorone diisocyanate, poly (1,6-hexanediol carbonate) having a number average molecular weight of 1000, polyoxytetramethylene glycol, neopentyl glycol, and dimethylolbutanoic acid neutralized with triethylamine having a number average molecular weight of 1000. The binding concentration of the aqueous dispersion of polycarbonate polyether polyurethane, urethane and urea was 1710 eq / ton.
-Polyether polyurethane: (u3)
A polyether polyurethane aqueous dispersion composed of isophorone diisocyanate, polyoxytetramethylene glycol having a number average molecular weight of 1000, neopentyl glycol, dimethylolpropionic acid neutralized with triethylamine, and the binding concentration of urethane and urea are: 3110 eq / ton.
・ Polyester polyurethane: (u4)
A polyester polyurethane aqueous dispersion composed of hydrogenated diphenyl diisocyanate, polyhexamethylene adipate, neopentyl glycol, dimethylolpropionic acid neutralized with triethylamine, and a binding concentration of urethane and urea of 3260 eq / ton.

・ Polyester resin: (e1)
Product name Finetex (registered trademark) ES-670 manufactured by DIC, which is an aqueous dispersion of an aromatic polyester
・ Crosslinking agent: (c1)
Methoxymethylol melamine DIC Corporation trade name Beccamin (registered trademark) J101
・ Crosslinking agent: (c2)
Oxazoline-based water-soluble resin cross-linking agent manufactured by Nippon Shokubai Co., Ltd. Trade name Epocross (registered trademark) WS-500
・ Crosslinking agent: (c3)
Product name Denacol (registered trademark) EX-521 manufactured by Nagase ChemteX Corporation
・ Fine particles: (d1)
Colloidal silica fine particles (average particle size 0.07μm)

  The film of the present invention can be suitably used as, for example, a base film used for an optical member or a solar cell back surface protective film.

Claims (3)

A film having a total nitrogen amount of 30 ppm or less, having a coating layer by in-line coating containing a polyurethane having at least one of a polycarbonate skeleton or a polyether skeleton and a crosslinking agent on at least one surface of a base polyester film, A biaxially oriented polyester film comprising 5% by weight or more of a self-regenerating raw material in the polyester film . The biaxially oriented polyester film according to claim 1, which has a lens layer on one surface via a coating layer. The biaxially oriented polyester film according to claim 1, further comprising an ethylene-vinyl acetate resin thermal laminate layer on one surface through an application layer.