JP2012025891A - Polyester film for double-sided self-adhesive sheet without substrate - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a mold-release film suppressing peeling rate dependency to the minimum when used in optical applications such as a touch panel, liquid crystal deflector plate and retardation plate, solving problems such as productivity and cost, and further reducing process contamination and foreign matter in the self-adhesive.SOLUTION: The polyester film has a coating layer obtained by coating a coating liquid containing polyvinyl alcohol, and on the coating layer, a silicone-based mold-release layer containing a silicone resin having an alkenyl group and an alkyl group as functional groups, a low molecular weight silicone compound with ≤1,000 molecular weight and a platinum-based catalyst. Low speed peeling force of the mold-release layer at 300 mm/min speed zone lies within the range of 10-20 mN/cm; and high speed peeling force thereof at 10,000 mm/min speed zone is 2.5 times that of low speed peeling force or less.

Description

  The present invention relates to a polyester film for a base-less double-sided pressure-sensitive adhesive sheet suitable for optical applications.

  Conventionally, various pressure-sensitive adhesive sheets for surface bonding between objects are known, and a base-less double-sided pressure-sensitive adhesive sheet is known as one of pressure-sensitive adhesive sheets. The substrate-less double-sided pressure-sensitive adhesive sheet is configured by laminating a light release sheet having a relatively low peeling force and a heavy release sheet having a relatively high peeling force on both sides of the pressure-sensitive adhesive layer, and removing the double-sided release sheet. The latter is a double-sided pressure-sensitive adhesive sheet that only has a pressure-sensitive adhesive layer that does not have a supporting substrate. The substrate-less double-sided PSA sheet is first peeled off from the light release sheet, and one side of the exposed PSA layer is bonded to the object surface. The other side of the layer is bonded to a different object surface, thereby surface bonding between the objects.

  In recent years, the use of a baseless double-sided pressure-sensitive adhesive sheet has been spreading, and is also used for members for various optical applications. For example, as the LCD member, peel off the release film with the lighter peeling force of the base-less double-sided pressure-sensitive adhesive sheet, paste the polarizing plate on the surface, and release the heavy release force on the opposite side. May be used.

  From the viewpoint of workability in production, processing at a certain high speed range can be considered, but in the case of a light release film, it is possible to achieve a light release force, but it is possible to increase the processing speed while achieving this. It is very difficult to simultaneously achieve that the difference in peel force between the release film and the heavy release film is not reduced. If the peel force difference with the heavy release film is reduced, there will be problems such as the film on both sides being peeled off at the same time in the peeling process, and the adhesive being peeled off together because the peel force difference is small. This will cause problems in workability and productivity.

  In addition, when a release polyester film is used for optical applications such as a polarizing plate base material in this way, an optical inspection for finding foreign matter or the like may be performed with the polarizing plate attached. For this reason, defects such as foreign matters have become more important than ever.

  As one of the causes of the generation of foreign substances, an oligomer (hereinafter sometimes abbreviated as OL) contained in a polyester film is considered. OL, which is considered to be a low molecular weight sublimate of polyester, is deposited on the surface of the film within the production process and adheres to a roll or the like that comes into contact with the film to become a foreign matter. Moreover, in order to reduce a foreign material, although the operation | work which removes the oligomer adhering to a roll is performed, the problem that production efficiency worsens is also mentioned.

JP 2009-220296 A JP 2003-231214 A JP 2002-361737 A Japanese Patent Application No. 2001-301024 Japanese Patent Application No. 2010-121101 JP 2009-220296 A JP 2010-13561 A Japanese Patent Laid-Open No. 10-158519

  The present invention has been made in view of the above circumstances, and the problem to be solved is that the substrate-less double-sided pressure-sensitive adhesive sheet has a peeling rate dependency in optical applications, for example, touch panels, liquid crystal deflecting plates, phase difference plates, and the like. To provide an inexpensive polyester film for double-sided pressure-sensitive adhesive sheets that eliminates problems such as productivity by minimizing process contamination and reducing foreign matter on adhesives. It is in.

  As a result of intensive studies in view of the above circumstances, the present inventors have found that the above problem can be easily solved by a polyester film having a specific configuration, and have completed the present invention.

  That is, the gist of the present invention is that a silicone resin having a functional group having an alkenyl group and an alkyl group on a coating layer of a polyester film having a coating layer obtained by coating a coating solution containing polyvinyl alcohol, and having a molecular weight. A polyester film having a silicone release layer containing a low molecular weight silicone compound having a molecular weight of 1000 or less and a platinum-based catalyst, and a low-speed peel force in a range of 300 mm / min of the release layer is in the range of 10 to 20 mN / cm. And the polyester film for a substrate-less double-sided pressure-sensitive adhesive sheet, wherein the high-speed peel force in the 10,000 mm / min speed region is 2.5 times or less of the low-speed peel force.

  According to the present invention, it is possible to provide a release polyester film having a small release rate dependency, and thus its industrial value is high.

  The polyester film referred to in the present invention is a film obtained by stretching a sheet melt-extruded from an extrusion die according to a so-called extrusion method.

The polyester constituting the film refers to a polymer containing an ester group obtained by polycondensation from dicarboxylic acid and diol or from hydroxycarboxylic acid.
Examples of dicarboxylic acids include terephthalic acid, isophthalic acid, adipic acid, azelaic acid, sebacic acid, 2,6-naphthalenedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, and diols include ethylene glycol and 1,4-butane. Examples include diol, diethylene glycol, triethylene glycol, neopentyl glycol, 1,4-cyclohexanedimethanol, polyethylene glycol and the like, and examples of hydroxycarboxylic acid include p-hydroxybenzoic acid and 6-hydroxy-2-naphthoic acid. be able to. Typical examples of such a polymer include polyethylene terephthalate and polyethylene-2,6-naphthalate.

  In the film of the present invention, it is preferable to blend particles mainly for the purpose of imparting slipperiness and preventing the occurrence of scratches in each step. The kind of the particle to be blended is not particularly limited as long as it is a particle capable of imparting slipperiness. Specific examples thereof include silica, calcium carbonate, magnesium carbonate, barium carbonate, calcium sulfate, calcium phosphate, and phosphoric acid. Examples of the particles include magnesium, kaolin, aluminum oxide, and titanium oxide. Further, heat-resistant organic particles as described in JP-B-59-5216, JP-A-59-217755 and the like may be used. Examples of other heat-resistant organic particles include thermosetting urea resins, thermosetting phenol resins, thermosetting epoxy resins, benzoguanamine resins, and the like. Furthermore, precipitated particles obtained by precipitating and finely dispersing a part of a metal compound such as a catalyst during the polyester production process can also be used.

  On the other hand, the shape of the particles to be used is not particularly limited, and any of a spherical shape, a block shape, a rod shape, a flat shape and the like may be used. Moreover, there is no restriction | limiting in particular about the hardness, specific gravity, a color, etc. These series of particles may be used in combination of two or more as required.

  Moreover, the average particle diameter of the particle | grains to be used is 0.01-3 micrometers normally, Preferably it is the range of 0.1-2 micrometers. When the average particle size is less than 0.01 μm, the slipperiness may not be sufficiently imparted. On the other hand, when the thickness exceeds 3 μm, transparency may be lowered due to the aggregate of the particles when the film is formed, and it is easy to cause breakage, which causes a problem in terms of productivity. There is.

  Furthermore, the content of particles in the polyester is usually in the range of 0.001 to 5% by weight, preferably 0.005 to 3% by weight. When the particle content is less than 0.001% by weight, the slipperiness of the film may be insufficient. On the other hand, when the content exceeds 5% by weight, the transparency of the film is insufficient. There is a case.

  The method for adding particles to the polyester layer is not particularly limited, and a conventionally known method can be adopted. For example, it can be added at any stage for producing the polyester constituting each layer, but it is preferably added after completion of esterification or transesterification.

  Also, a method of blending a slurry of particles dispersed in ethylene glycol or water with a vented kneading extruder and a polyester raw material, or a blending of dried particles and a polyester raw material using a kneading extruder. It is done by methods.

  In addition to the above-mentioned particles, conventionally known antioxidants, antistatic agents, thermal stabilizers, lubricants, dyes, pigments, and the like can be added to the polyester film in the present invention as necessary.

  Although the thickness of the polyester film in this invention will not be specifically limited if it is a range which can be formed into a film as a film, Usually, 10-350 micrometers, Preferably it is the range of 15-100 micrometers.

  Next, although the manufacture example of the polyester film in this invention is demonstrated concretely, it is not limited to the following manufacture examples at all. That is, a method of using the polyester raw material described above and cooling and solidifying a molten sheet extruded from a die with a cooling roll to obtain an unstretched sheet is preferable. 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, and an electrostatic application adhesion method and / or a liquid application adhesion method is preferably employed. Next, the obtained unstretched sheet is stretched in the biaxial direction. In that case, first, the unstretched sheet is stretched in one direction by a roll or a tenter type stretching machine. The stretching temperature is usually 90 to 140 ° C., preferably 95 to 120 ° C., and the stretching ratio is usually 2.5 to 7 times, preferably 3.0 to 6 times. Next, the film is stretched in the direction perpendicular to the first stretching direction. In that case, the stretching temperature is usually 90 to 170 ° C., and the stretching ratio is usually 3.0 to 7 times, preferably 3.5 to 6 times. is there. Subsequently, heat treatment is performed at a temperature of 180 to 270 ° C. under tension or under relaxation within 30% to obtain a biaxially oriented film. In the above-described stretching, a method in which stretching in one direction is performed in two or more stages can be employed. In that case, it is preferable to carry out so that the draw ratios in the two directions finally fall within the above ranges.

  For the production of the polyester film of the present invention, a simultaneous biaxial stretching method can also be employed. The simultaneous biaxial stretching method is a method in which the unstretched sheet is usually stretched and oriented in the machine direction and the width direction at 90 to 140 ° C., preferably 80 to 110 ° C., and the stretching ratio is as follows. Is 4 to 50 times, preferably 7 to 35 times, and more preferably 10 to 25 times in terms of area magnification. Subsequently, heat treatment is performed at a temperature of 170 to 250 ° C. under tension or under relaxation within 30% to obtain a stretched oriented film. With respect to the simultaneous biaxial stretching apparatus that employs the above-described stretching method, a conventionally known stretching method such as a screw method, a pantograph method, or a linear driving method can be employed.

  Next, formation of the coating layer for the purpose of OL sealing which comprises the polyester film of this invention is demonstrated. As for the coating layer, it may be provided by in-line coating, which treats the film surface during the stretching process of the polyester film, or may be applied off-system on the film once manufactured, and may employ both offline coating. You may use together. In-line coating is preferably used in that it can be applied at the same time as film formation, and thus can be manufactured at low cost, and the thickness of the coating layer can be changed by the draw ratio.

  The in-line coating is not limited to the following, but for example, in the sequential biaxial stretching, the coating treatment can be performed particularly before the lateral stretching after the longitudinal stretching is finished. When a coating layer is provided on a polyester film by in-line coating, coating can be performed simultaneously with film formation, and the coating layer can be processed at a high temperature, and a film suitable as a polyester film can be produced.

  In the present invention, it is normal to use a binder polymer in the coating layer. The binder polymer is a gel permeation according to a high molecular compound safety evaluation flow scheme (sponsored by the Chemical Substance Council in November 1985). It is defined as a high molecular compound having a number average molecular weight (Mn) of 1000 or more as measured by ablation chromatography (GPC) and having film-forming properties.

  Analysis of the components in the coating layer can be performed by surface analysis such as TOF-SIMS.

  When providing a coating layer by in-line coating, the above-mentioned series of compounds is applied as an aqueous solution or dispersion, and the coating solution adjusted to a solid content concentration of about 0.1 to 50% by weight as a guide is applied onto the polyester film. It is preferable to produce a laminated polyester film. Moreover, in the range which does not impair the main point of this invention, a small amount of organic solvents may be contained in the coating liquid for the purpose of improving dispersibility in water, improving film-forming properties, and the like. Only one type of organic solvent may be used, or two or more types may be used as appropriate.

  In order to achieve the above object, in the present invention, an oligomer precipitation preventing layer is formed on the film surface by coating, and the layer comprises 10 to 100% by weight of polyvinyl alcohol, preferably 20 to 90% by weight, more preferably 30 to 30%. It shall contain 90% by weight. If the content of polyvinyl alcohol is less than 10% by weight, the oligomer sealing effect is insufficient, which is not preferable.

  The polyvinyl alcohol used in the present invention can be synthesized by a normal polymerization reaction and is preferably water-soluble. The degree of polymerization of polyvinyl alcohol is not particularly limited, but is usually 100 or more, preferably 300 to 40,000. When the degree of polymerization is 100 or less, the water resistance of the coating layer tends to decrease. The degree of saponification of the polyvinyl alcohol used in the present invention is not particularly limited, but a polyvinyl acetate saponified product that is usually 70 mol% or more, preferably 80 mol% or more and 99.9 mol% or less is practically used. It is done.

  In the oligomer precipitation preventing layer in the present invention, a water-soluble or water-dispersible binder resin other than the above-mentioned polyvinyl alcohol may be used in combination as necessary. Examples of the binder resin include polyester, polyurethane, acrylic resin, vinyl resin, epoxy resin, amide resin, acrylate resin, and the like. In these, each skeleton structure may have a composite structure substantially by copolymerization or the like. Examples of the binder resin having a composite structure include acrylic resin graft polyester, acrylic resin graft polyurethane, vinyl resin graft polyester, vinyl resin graft polyurethane, and acrylate resin graft polyethylene glycol. The blending amount of the binder component is preferably 50 parts by weight or less, and more preferably 30 parts by weight or less, by weight with respect to the coating layer. Furthermore, the coating layer of the film of the present invention may contain a crosslinking reactive compound as required.

  Crosslinking reactive compounds include methylolated or alkylolated urea, melamine, guanamine, acrylamide, polyamide and other compounds, polyamines, epoxy compounds, oxazoline compounds, aziridine compounds, blocked isocyanate compounds, silane cups Polyfunctional low molecular weight compounds such as ring agents, titanium coupling agents, zirco-aluminate coupling agents, metal chelates, organic acid anhydrides, organic peroxides, thermally or photoreactive vinyl compounds and photosensitive resins, and It is selected from polymer compounds.

  Crosslinkable compounds improve the cohesiveness, surface hardness, scratch resistance, solvent resistance, and water resistance of the easy-adhesive resin layer mainly by cross-linking reaction with the functional groups of the resin contained in the easy-adhesive resin layer. can do. For example, when the functional group of the easily adhesive resin is a hydroxyl group, the crosslinking reactive compound is preferably a melamine compound, a blocked isocyanate compound, an organic acid anhydride, or the like, and the functional group of the easily adhesive polyester is an organic acid or an anhydride thereof. In this case, epoxy-based compounds, melamine-based compounds, oxazoline-based compounds, metal chelates and the like are preferable as the cross-linking reactive compound. It is preferable to select and use a functional group contained in the easily adhesive resin and one having a high crosslinking reaction efficiency. Examples of the melamine compound in the present invention include methoxymethylated melamine and butoxymethylated melamine which are alkylol or alkoxyalkylolated melamine compounds, and those obtained by co-condensing urea or the like with a part of melamine can also be used. .

The cross-linking reactive compound may be either a low molecular weight compound or a high molecular polymer having a reactive functional group as long as the reactive functional group is always contained in two or more functional groups in one molecule. The compounding amount of the crosslinking reactive compound is preferably 50 parts by weight or less, more preferably 30 parts by weight or less, and particularly preferably 15 parts by weight or less in terms of parts by weight with respect to the easily adhesive resin layer.
Furthermore, the easily adhesive resin layer of the present invention may contain inert particles for improving the slipperiness of the coating layer, if necessary.

  Examples of the inert particles include inorganic inert particles and organic inert particles. Examples of the inorganic inert particles include silica sol, alumina sol, calcium carbonate, and titanium oxide. Examples of the organic inert particles include fine particles containing a single or copolymer of polystyrene resin, polyacrylic resin, and polyvinyl resin, or organic particles represented by crosslinked particles in which these and a crosslinking component are combined. These inert particles preferably have a softening temperature or decomposition temperature of about 200 ° C. or higher, more preferably 250 ° C. or higher, particularly 300 ° C. or higher. The average particle diameter (d) of the inert particles is 1/3 ≦ d / L ≦ 3, and further 1/2 ≦ d / L ≦ 2, when the average film thickness of the easily adhesive resin layer is (L). It is preferable to select so as to satisfy the relationship.

  The OL sealing layer of the present invention comprises a surfactant, an antifoaming agent, a coating property improver, a thickener, a low molecular antistatic agent, an organic lubricant, an antioxidant, an ultraviolet absorber, and foam as necessary. A small amount of additives such as additives, dyes and pigments may be contained. These additives may be used alone or in combination of two or more as necessary. The coating layer of the film of the present invention may be formed only on one side of the polyester film or on both sides. In the case of forming only on one side, another type of coating layer can be formed on the opposite side as required, and further properties can be imparted. In addition, in order to improve the applicability | paintability and adhesiveness to the film of a coating liquid, you may give a chemical process, an electrical discharge process, etc. to the film before application | coating.

Respect polyester film of the present invention, the thickness of the coating layer provided on the polyester film is usually 0.002~1.0g / ^{m 2,} more preferably 0.005 to 0.5 / ^{m 2,} more preferably 0 The range is from 0.01 to 0.2 g / m ² . If the film thickness is less than 0.002 g / m ^2, sufficient adhesion may not be obtained, and if it exceeds 1.0 g / m ² , the appearance, transparency, and film blocking properties may be deteriorated. There is sex.

  In the polyester film of the present invention, examples of the method for providing the coating layer include conventionally known coating methods such as reverse gravure coating, direct gravure coating, roll coating, die coating, bar coating, and curtain coating. Regarding the coating method, there is a description example in “Coating method” published by Yasuharu Harasaki in 1979.

  In the present invention, the drying and curing conditions for forming the coating layer on the polyester film are not particularly limited. For example, when the coating layer is provided by off-line coating, it is usually 3 to 80 to 200 ° C. The heat treatment may be performed for 40 seconds, preferably 100 to 180 ° C. for 3 to 40 seconds.

  On the other hand, when the coating layer is provided by in-line coating, heat treatment is usually performed at 70 to 280 ° C. for 3 to 200 seconds as a guide.

  Further, irrespective of off-line coating or in-line coating, heat treatment and active energy ray irradiation such as ultraviolet irradiation may be used in combination as required. The polyester film constituting the laminated polyester film in the present invention may be subjected to surface treatment such as corona treatment or plasma treatment in advance.

  The OL sealing layer of the polyester film of the present invention is preferably formed by blending a binder resin and a crosslinking agent in an arbitrary ratio. In this case, since the layer forms a barrier layer densely, the OL is suppressed. be able to. For this reason, there is an effect that OL from the polyester film is not attached to the adhesive as much as possible and is not produced in the previous processing step. Therefore, both sides of the OL sealing layer of the polyester film of the present invention are preferable, and it is necessary to apply at least one side according to the application.

  In the present invention, OL (oligomer) is defined as a cyclic trimer among low molecular weight substances that crystallize and precipitate on the film surface after heat treatment.

After heat-treating the polyester film of the present invention (180 ° C., 10 minutes), the amount of OL extracted from the coating layer surface with dimethylformamide is preferably 3.0 mg / m ² or less, more preferably 1.0 mg. / M ² or less. When OL exceeds 3.0 mg / m ² , there is a process contamination, and when the pressure-sensitive adhesive is bonded, a foreign matter may be generated and a product yield may be deteriorated.

  The release layer formed on the coating layer of the film of the present invention is not particularly limited as long as it contains a material having releasability. Among them, the one containing a curable silicone resin is preferable because the releasability is improved. A type having a curable silicone resin as a main component may be used, or a modified silicone type by graft polymerization with an organic resin such as a urethane resin, an epoxy resin, or an alkyd resin may be used.

  As the type of the curable silicone resin, any of the curing reaction types such as an addition type, a condensation type, an ultraviolet ray curable type, an electron beam curable type, and a solventless type can be used.

  Examples of silicone resins having an alkenyl group and an alkyl group as functional groups used in the present invention include the following. First, a curable silicone resin containing an alkenyl group is a diorganopolysiloxane having a trimethylsiloxy group-blocked dimethylsiloxane / methylhexenylsiloxane copolymer (96 mol% dimethylsiloxane unit, 4 mol% methylhexenylsiloxane unit). , Dimethylvinylsiloxy group-blocked dimethylsiloxane / methylhexenylsiloxane copolymer (97 mol% dimethylsiloxane unit, 3 mol% methylhexenylsiloxane unit), dimethylsiloxane / methylhexenyl blocked with dimethylhexenylsiloxy group blocked at both ends of the molecular chain Siloxane copolymers (95 mol% of dimethylsiloxane units and 5 mol% of methylhexenylsiloxane units) can be mentioned. As the molecular polysiloxane, molecular chain both ends trimethylsiloxy group-capped methylhydrogenpolysiloxane, molecular chain both ends trimethylsiloxy group-capped dimethylsiloxane / methylhydrogensiloxane copolymer, molecular chain both ends dimethylhydrogensiloxy group-capped methyl Examples thereof include hydrogen polysiloxane and dimethylhydrogensiloxy group-blocked dimethylsiloxane / methylhydrogensiloxane copolymer having both molecular chain terminals.

  Examples of the low molecular weight silicone compound having a molecular weight of 1000 or less used in the present invention include the following. That is, hexamethylcyclotrisiloxane, octamethylcyclotetrasiloxane, decamethylcyclopentasiloxane and the like can be mentioned. Further, in addition to the former low molecular weight cyclic siloxane, molecular chain both-end trimethylsiloxy group-capped dimethylsiloxane oligomer; molecular chain both-end dimethylhydroxysiloxy group-capped dimethylsiloxane oligomer and the like may be mixed as necessary. These low-molecular cyclic siloxanes are preferably contained in the silicone resin as a migration component in an amount of 0.1 to 5.0% by weight. By having a low molecular component such as cyclic siloxane, desired light peeling can be achieved.

  As mentioned above, specific examples of silicone resin coatings include KS-774, KS-775, KS-778, KS-779H, KS-847H, KS-856, and X-62-2422 manufactured by Shin-Etsu Chemical Co., Ltd. , X-62-2461, DKQ3-202, DKQ3-203, DKQ3-204, DKQ3-205, DKQ3-210, manufactured by Dow Corning Asia Co., Ltd., YSR-3022, TPR-6700, manufactured by Toshiba Silicone Co., Ltd. TPR-6720, TPR-6721, Toray Dow Corning Co., Ltd. LTC300B, LTC303E, LTC310, LTC314, SRX357, BY24-749, SD7333, BY24-179, SP7015, SP7259, SD7220, SD7226, SD7229, etc. . Further, a release control agent may be used in combination to adjust the release property of the release layer. Further, as described above, a silane compound having an amino group may be added to the release layer.

  In the present invention, as a method for providing a release layer on the polyester film, a conventionally known coating method such as reverse roll coating, gravure coating, bar coating, doctor blade coating, or the like can be used. The coating amount of the release layer in the present invention is usually in the range of 0.01-1 g / m2.

  In the present invention, a coating layer such as an adhesive layer, an antistatic layer and an oligomer precipitation preventing layer may be provided on the surface where the release layer is not provided, and the polyester film may be subjected to corona treatment, plasma treatment, etc. A surface treatment may be applied.

  Moreover, drying and / or curing (thermal curing, ionizing radiation curing, etc.) of the coating film of the pressure-sensitive adhesive layer or the release layer can be performed individually or simultaneously. When performing simultaneously, it is preferable to carry out at the temperature of 80 degreeC or more. The drying and curing conditions are preferably 80 ° C. or higher and 10 seconds or longer. When the drying temperature is less than 80 ° C. or the curing time is less than 10 seconds, the coating film is not completely cured, and the coating film tends to fall off, which is not preferable.

  In the polyester film of the present invention, a platinum-based catalyst that promotes an addition-type reaction is used in order to make the coating layer clean and strong. As this component, chloroplatinic acid, alcohol solution of chloroplatinic acid, a complex of chloroplatinic acid and olefin, a platinum compound such as a complex of chloroplatinic acid and alkenylsiloxane, platinum black, platinum-supported silica, platinum-supported activated carbon Is exemplified. The platinum-based catalyst content in the coating layer is usually 0.3 to 3.0% by weight, preferably 0.5 to 2.0% by weight. If the platinum-based catalyst content in the coating layer is lower than 0.3% by weight, it may cause problems such as deterioration of the surface condition due to insufficient peeling force and insufficient curing reaction in the coating layer. On the other hand, if the platinum-based catalyst content in the coating layer exceeds 3.0% by weight, it may be costly, and the reactivity may increase and process defects such as generation of gel foreign matter may occur. is there.

  In addition, since the addition-type reaction is very reactive, acetylene alcohol may be added as an unreactive inhibitor in some cases. The component is an organic compound having a carbon-carbon triple bond and a hydroxyl group, and preferably 3-methyl-1-butyn-3-ol, 3,5-dimethyl-1-hexyn-3-ol and phenylbuty It is a compound selected from the group consisting of nor.

  In the present invention, the peeling force refers to a double-sided pressure-sensitive adhesive tape (“No. 31B” manufactured by Nitto Denko) attached to the release layer surface and left at room temperature for 1 hour, and then the substrate film and the peeling angle of 180 °. The value measured with a tensile tester when the tape is peeled off at the tensile speed. The method for adjusting the specific peeling force in the present invention can be achieved by selecting the composition in the release layer, but other means can also be adopted, mainly the type of release agent for the silicone release layer. Is preferably changed according to the desired peeling force, and furthermore, since the peeling force largely depends on the application amount of the release agent to be used, a method of adjusting the application amount of the release agent is more preferable.

  The value of the peeling force of the polyester film in the present invention is in the range of 10 to 20 mN / cm in the 300 mm / min speed range. When the peeling force is less than 10 mN / cm, the peeling force becomes too light, and the problem of peeling easily occurs even in a scene where it is not necessary to peel. When the peel force exceeds 20 mN / cm, the difference in peel force between the release film with the larger peel force becomes smaller, causing problems in the peel process, and the selection width of the release film with the greater peel force is There are problems such as narrowing.

  Furthermore, it is necessary that the peeling force in the 10,000 mm / min speed region taking into consideration workability is 2.5 times or less of the above peeling force. If the peel force ratio is greater than 2.5 times, the peel force difference between the release film and the heavier peel force will be small, and the peel process will not be successful, or the adhesive will peel off. It causes a defect.

  EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited to a following example, unless the summary is exceeded. The measurement method and evaluation method used in the present invention are as follows.

(1) Measurement of intrinsic viscosity of polyester 1 g of polyester from which other polymer components and pigments incompatible with polyester have been removed are precisely weighed, and 100 ml of a mixed solvent of phenol / tetrachloroethane = 50/50 (weight ratio) is added. It was dissolved and measured at 30 ° C.

(2) Measurement of average particle size (d50: μm) 50% integrated (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) Measurement of transmittance of polyester film According to JIS-K7105, the total light transmittance of the polyester film was measured with an integrating sphere turbidimeter NDH-300A manufactured by Nippon Denshoku Industries Co., Ltd. Judgment is based on the following criteria.

(4) Measurement of haze (turbidity) of polyester film According to JIS-K7105, the haze of the film was measured with an integrating sphere turbidimeter NDH-20D manufactured by Nippon Denshoku Industries Co., Ltd.

(5) Measurement of heat shrinkage rate of polyester film The polyester film was sampled at an arbitrary length L (cm) in the longitudinal direction (hereinafter abbreviated as MD) and the lateral width direction (hereinafter abbreviated as TD). To do. Subsequently, the sample is heated in an oven at 160 ° C. for 5 minutes, and the sample is taken out of the oven and the length l (cm) is measured. This operation is performed three times, and the average value is adopted as the value of the heat shrinkage rate. The heat shrinkage rate can be calculated by the following formula.
Heat shrinkage (%) = {(L−l) / L} × 100

(6) Measurement of catalyst amount in coating layer Using SAICAS, the sample film was obliquely cut to expose the cross section. afterwards,
The amount of catalyst containing platinum contained in the polyester film coating layer was determined using TOF-SIMS (time-of-flight mass spectrometry mass spectrum).

(7) Evaluation of release film release force (F) After attaching one side of a double-sided adhesive tape (Nitto Denko “No. 502”) to the surface of the release layer of the sample film, cut into a size of 50 mm × 300 mm After that, the peel strength after standing for 1 hour at room temperature is measured. The peeling force was measured using a tensile tester (“Intesco Model 2001” manufactured by Intesco Corporation) at a tensile speed of 300 mm / min. And 10,000 mm / min. The film was peeled 180 ° under the conditions. Judgment is based on the following criteria.

<Peeling force at 300 mm / min>
○: Range of 10 to 20 mN / cm ×: Less than 10 mN / cm or greater than 20 mN / cm

<Comparison of peel force at 10,000 mm / min and peel force at 300 mm / min>
Judgment was made based on the value obtained by the following equation.
(10000 mm / min peeling force (mN / cm)) / (300 mm / min peeling force (mN / cm))
○: 2.5 or less ×: More than 2.5

(8) Measurement of OL extracted from anchor layer surface An unheat-treated release film is heated in air at 180 ° C. for 10 minutes in advance. After that, the heat-treated film is brought into close contact with the inner surface of a box having a top and width of 10 cm and a height of 3 cm, and the box shape is obtained. When the coating layer is provided, the coating layer surface is set to the inside. Next, 4 ml of DMF (dimethylformamide) is placed in the box prepared by the above method and left for 3 minutes, and then DMF is recovered. The recovered DMF was supplied to liquid chromatography (manufactured by Shimadzu Corporation: LC-7A) to determine the amount of OL in DMF, and this value was divided by the area of the film in contact with DMF to obtain the amount of film surface OL (mg / M ² ).

  The amount of oligomer in DMF was determined from the peak area ratio between the standard sample peak area and the measured sample peak area (absolute calibration curve method). The standard sample was prepared by accurately weighing OL (cyclic trimer) collected in advance and dissolving it in DMF accurately weighed. The concentration of the standard sample is preferably in the range of 0.001 to 0.01 mg / ml. The conditions for the liquid chromatograph were as follows.

Mobile phase A: Acetonitrile Mobile phase B: 2% acetic acid aqueous solution Column: “MCI GEL ODS 1HU” manufactured by Mitsubishi Chemical Corporation
Column temperature: 40 ° C
Flow rate: 1 ml / min Detection wavelength: 254 nm

(9) Release characteristics The release characteristics were evaluated from the situation when the release film was peeled off from the laminated film having the adhesive layer.
○: The release film peels cleanly, and the phenomenon that the adhesive adheres to the release layer is not observed. Δ: The release film peels off, but the adhesive adheres to the release layer when peeled at a high speed. Adhesive adheres to the release film and does not peel off well.

(10) Comprehensive evaluation An evaluation is performed in consideration of all film forming properties, productivity, and inspection characteristics. Judgment is based on the following criteria.
○: Even if produced, it can be supplied as a product. Further, the OL amount is less than 1.0 mg / m ² .
Δ: Productivity is good and the frequency of defects is low. Further, the OL amount is less than 1.0 mg / m ² .
X: Productivity is poor. Many troubles occur. The OL amount is more than 1.0 mg / m ² .

The polyester used in the examples and comparative examples was prepared as follows.
<Method for producing polyester (a)>
Using 100 parts by weight of dimethyl terephthalate and 60 parts by weight of ethylene glycol as starting materials, adding tetrabutoxy titanate as a catalyst to the reactor, setting the reaction start temperature to 150 ° C., and gradually increasing the reaction temperature as methanol is distilled off. It was 230 degreeC after 3 hours. After 4 hours, the transesterification reaction was substantially completed, and then a polycondensation reaction was performed 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 0.61 due to a change in the stirring power of the reaction vessel, and the polymer was discharged under nitrogen pressure to obtain a polyester (a) having an intrinsic viscosity of 0.61.

<Method for producing polyester (b)>
In the method for producing polyester (a), after adding ethyl acid phosphate, an ethylene glycol slurry of synthetic calcium carbonate particles having an average particle diameter of 0.8 μm was added so that the content of the particles with respect to polyester was 1% by weight. Obtained polyester (b) using the method similar to the manufacturing method of polyester (a). The obtained polyester (b) had an intrinsic viscosity of 0.60.

<Production of polyester (c)>
Starting from 100 parts by weight of dimethyl terephthalate and 60 parts by weight of ethylene glycol, magnesium acetate tetrahydrate is added as a catalyst to the reactor, the reaction start temperature is 150 ° C., and the reaction temperature is gradually increased as methanol is distilled off. The temperature was raised to 230 ° C. after 3 hours. After 4 hours, the transesterification reaction was substantially terminated. Ethyl acid phosphate was added to the reaction mixture, which was then transferred to a polycondensation tank, and 0.04 part of antimony trioxide was added to carry out a polycondensation reaction 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 0.45 due to a change in stirring power of the reaction tank, and the polymer was discharged under nitrogen pressure to obtain a polyester chip (c). The intrinsic viscosity of this polyester was 0.45.

<Manufacture of polyester (d)>
The intrinsic viscosity of this polyester chip was increased by a solid phase polycondensation method. After treatment in a preliminary crystallization tank at 170 ° C. in a nitrogen atmosphere for 0.5 hours, the moisture content becomes 0.005% at a temperature of 200 ° C. using a tower dryer that flows an inert gas. Until dried. Thereafter, it was sent to a solid phase polymerization tank and subjected to solid phase polymerization at 240 ° C. for 3 hours to obtain a polyester (d) having an intrinsic viscosity of 0.70.

<Manufacture of polyester (e)>
When producing the polyester (d), solid phase polymerization was performed in a solid phase polymerization tank for 5 hours to obtain a polyester (e) having an intrinsic viscosity of 0.80.

Example 1:
<Manufacture of polyester film>
As a raw material for the surface layer, 70% by weight of polyester (e) and 30% by weight of polyester (b) are mixed. As a raw material for the intermediate layer, 84% by weight of polyester (a) and 16% by weight of polyester (b) are mixed. Each was supplied to an extruder with a vent and melt-extruded at 290 ° C., and then cooled and solidified on a cooling roll having a surface temperature set to 40 ° C. using an electrostatic application adhesion method to obtain an unstretched sheet. Next, the film was stretched 2.8 times in the longitudinal direction at 100 ° C., and then the following coating agent was applied to one side of the longitudinally stretched film so that the coating amount (after drying) was 0.03 g / m ² . After that, the film was guided to a tenter and transversely stretched at 120 ° C., preheated in the tenter and subjected to a transverse stretch of 5.1 times at 120 ° C., then heat-treated at 220 ° C. for 10 seconds, and then at 180 ° C. 4% relaxation was applied in the direction to obtain a master roll having a width of 4000 mm. A slit was made from a position of 1400 mm from the end of the master roll, and the core roll was wound up 1000 m to obtain a polyester film. The total thickness of the obtained film was 38 μm (layer constitution: surface layer 4 μm / intermediate layer 30 μm / surface layer 4 μm).

In addition, the example of a compound which comprises an application layer is as follows.
(Example compounds)
-Polyvinyl alcohol binder polymer having a saponification degree of 88 mol% and a polymerization degree of 350: A
Emulsion polymer of methyl methacrylate / ethyl acrylate / acrylonitrile / N-methylol methacrylamide = 45/45/5/5 (molar ratio) (emulsifier: anionic surfactant) Binder polymer: B
・ Crosslinking agent Hexamethoxymelamine crosslinking agent: C
・ Particulate colloidal silica (average particle diameter: 70 nm): D
Solid content ratio: A / B / C / D = 30/24/42/4

On the coating layer of the obtained polyester film, a release agent composed of release agent composition-A shown below was applied by a reverse gravure coating method so that the application amount (after drying) was 0.12 g / m ^2. A roll-shaped release polyester film was obtained under the conditions of a dryer temperature of 120 ° C. and a line speed of 30 m / min. The obtained release polyester film has a release force of 14 mN / cm at a speed of 300 mm / minute, a release force of 32 mN / cm at a speed of 10,000 mm / minute, and an OL amount of 0.82 mg / minute. It was m ^2.

<Releasing agent composition-A>
Curable silicone resin (LTC303E: manufactured by Toray Dow Corning) 20 parts Octamethylcyclotetrasiloxane (LTC303E: manufactured by Toray Dow Corning) 0.5 parts Addition type platinum catalyst (SRX212: manufactured by Toray Dow Corning) 0.16 Parts (0.8 wt%, 79 ppm)
MEK / toluene / n-heptane mixed solvent (mixing ratio is 1: 1: 1)

  For the obtained polyester film, a polarizing plate was prepared by the following method, and the peeling characteristics were evaluated. The obtained release film was peeled off cleanly, and the phenomenon that the adhesive adhered to the release layer was not observed.

<Manufacture of polarizing plate with release film>
The acrylic adhesive shown below is applied to the polarizing plate so that the thickness after drying is 25 μm, and after passing through a 130 ° C. drying oven in 30 seconds, the release film is bonded, and the adhesive is interposed. Thus, a polarizing plate with a release film in which the release film and the polarizing film were adhered to each other was prepared. The laminating direction of the film was performed so that the width direction of the release film was parallel to the orientation axis of the polarizing film.
Acrylic adhesive coating solution Acrylic adhesive (Olivein BPS429-4: manufactured by Toyo Ink) 100 parts Curing agent (BPS8515: manufactured by Toyo Ink) 3 parts MEK / toluene mixed solvent (mixing ratio is 1: 1) 50 parts

Examples 2-5:
In Example 1, the coating amount (after drying) of the release layer composition in the coating layer is changed to change the coating amount (after drying) of the OL sealing layer at the time of polyester film production. ) Was produced in the same manner as in Example 1 except that a polyester film was obtained. The obtained results are summarized in Table 1 below.

Comparative Examples 1-5:
In Example 1, the coating amount (after drying) of the release layer composition in the coating layer is changed to change the coating amount (after drying) of the OL sealing layer at the time of polyester film production. ) Was produced in the same manner as in Example 1 except that a polyester film was obtained. The results obtained are summarized in Table 2 below.

（※１）粘着加工工程内でのロールを中心とした汚染が激しく、粘着剤内にて異物が多く発生する。

(* 1) Contamination with a focus on rolls in the adhesive processing process is severe, and many foreign substances are generated in the adhesive.

  The polyester film of the present invention has good productivity and productivity by reducing foreign matter to process contamination and adhesive in the field of substrate-less double-sided pressure-sensitive adhesive sheet in optical applications where demand is great. Can be suitably used as a release polyester film having a small size.

Claims (2)

On the coating layer of the polyester film having a coating layer obtained by coating a coating solution containing polyvinyl alcohol, a silicone resin having an alkenyl group and an alkyl group as a functional group, a low molecular weight silicone compound having a molecular weight of 1000 or less, And a polyester film having a silicone-based release layer containing a platinum-based catalyst, the release layer has a low-speed peel force in the range of 300 mm / min and a range of 10 to 20 mN / cm, and 10000 mm / min. A polyester film for a substrate-less double-sided pressure-sensitive adhesive sheet, wherein a high-speed peel force in a speed range is 2.5 times or less of the low-speed peel force. The polyester film for a substrate-less double-sided pressure-sensitive adhesive sheet according to claim 1, wherein the low molecular weight silicone compound in the silicone release layer is a cyclic siloxane.