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WO2012090762A1 - Mold release film - Google Patents

Mold release film Download PDF

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Publication number
WO2012090762A1
WO2012090762A1 PCT/JP2011/079373 JP2011079373W WO2012090762A1 WO 2012090762 A1 WO2012090762 A1 WO 2012090762A1 JP 2011079373 W JP2011079373 W JP 2011079373W WO 2012090762 A1 WO2012090762 A1 WO 2012090762A1
Authority
WO
WIPO (PCT)
Prior art keywords
film
release
layer
mold release
release layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2011/079373
Other languages
French (fr)
Japanese (ja)
Inventor
齋藤智久
有馬奈美
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Plastics Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP2010289047A external-priority patent/JP2012137568A/en
Priority claimed from JP2011017375A external-priority patent/JP2012159548A/en
Priority claimed from JP2011069055A external-priority patent/JP2012179888A/en
Application filed by Mitsubishi Plastics Inc filed Critical Mitsubishi Plastics Inc
Priority to CN201180057701.3A priority Critical patent/CN103229080B/en
Priority to KR1020137011397A priority patent/KR101707863B1/en
Publication of WO2012090762A1 publication Critical patent/WO2012090762A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/56Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
    • B29C33/68Release sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/56Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
    • B29C33/60Releasing, lubricating or separating agents
    • B29C33/62Releasing, lubricating or separating agents based on polymers or oligomers
    • B29C33/64Silicone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/28Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42
    • B32B27/283Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42 comprising polysiloxanes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/04Interconnection of layers
    • B32B7/06Interconnection of layers permitting easy separation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/04Interconnection of layers
    • B32B7/12Interconnection of layers using interposed adhesives or interposed materials with bonding properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2255/00Coating on the layer surface
    • B32B2255/10Coating on the layer surface on synthetic resin layer or on natural or synthetic rubber layer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2255/00Coating on the layer surface
    • B32B2255/26Polymeric coating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/718Weight, e.g. weight per square meter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/748Releasability
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2457/00Electrical equipment
    • B32B2457/20Displays, e.g. liquid crystal displays, plasma displays
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2457/00Electrical equipment
    • B32B2457/20Displays, e.g. liquid crystal displays, plasma displays
    • B32B2457/208Touch screens
    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F2202/00Materials and properties
    • G02F2202/28Adhesive materials or arrangements

Definitions

  • the present invention relates to a release film, and more particularly to a release film used for a substrate-less double-sided pressure-sensitive adhesive sheet suitable for optical applications.
  • 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.
  • the baseless double-sided pressure-sensitive adhesive sheet has been used for various optical applications and the like.
  • 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.
  • Patent Document 1 In terms of workability in production, processing in a high speed range can be considered to some extent, but in the release film of light release, of course, to achieve a light release force, It is very difficult to simultaneously achieve that the difference in peel force from the release film that is as heavy as possible is not reduced (Patent Document 1). 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 (Patent Document 2).
  • Patent Documents 1 and 2 It is very difficult to control the above difference in peeling force, and various selection and control of the silicone component are necessary (Patent Documents 1 and 2), and it is also considered necessary to control the hardness of the silicone coating film.
  • one of the foreign substances described above may be caused by a low molecular component called an oligomer derived from a polyester film. If this oligomer can be prevented, the above-mentioned foreign matter malfunction during production can be suppressed, and the film and the subsequent process contamination can be prevented.
  • the oligomer (OL) is defined as a cyclic trimer among low molecular weight substances that crystallize after heat treatment and precipitate on the film surface.
  • JP 2009-220696 A Japanese Patent Laid-Open No. 10-158519 JP 2003-231214 A
  • 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 depends on the peeling rate when used in optical applications, for example, touch panels, liquid crystal deflecting plates, retardation plates, and the like. It is possible to minimize productivity, solve problems such as productivity, cost, etc., and provide oligomers with preventability and inspection properties, thereby reducing process contamination and foreign substances to adhesives.
  • the object is to provide an inexpensive release film.
  • the present inventor has found that the above problem can be easily solved by a polyester film having a release layer having a specific configuration, and has completed the present invention.
  • the gist of the present invention is a release film composed of a polyester film provided with a release layer, which is used by laminating the release layer to the adhesive layer of the base-less double-sided pressure-sensitive adhesive sheet.
  • the release film is characterized in that the high-speed peeling force is 2.5 times or less of the low-speed peeling force.
  • the layer structure of the preferable aspect of this invention has a coating layer obtained by apply
  • the polyester film which is the base material of the release film of 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.
  • Dicarboxylic acids include terephthalic acid, isophthalic acid, adipic acid, azelaic acid, sebacic acid, 2,6-naphthalenedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, etc.
  • diols include ethylene glycol, 1,4-butane. Examples include diol, diethylene glycol, triethylene glycol, neopentyl glycol, 1,4-cyclohexanedimethanol, and polyethylene glycol.
  • hydroxycarboxylic acid examples include p-hydroxybenzoic acid and 6-hydroxy-2-naphthoic acid. be able to.
  • Typical examples of such polymers include polyethylene terephthalate and polyethylene-2,6-naphthalate.
  • 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.
  • the particles include magnesium, kaolin, aluminum oxide, and titanium oxide.
  • 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.
  • 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.
  • the shape of the particles 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
  • the average particle diameter of the particles is usually in the range of 0.01 to 3 ⁇ m, preferably 0.1 to 2 ⁇ m.
  • the slipperiness may not be sufficiently imparted.
  • the thickness exceeds 3 ⁇ m, 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.
  • the particle content is usually in the range of 0.001 to 5% by weight, preferably 0.005 to 3% by weight.
  • the slipperiness of the film may be insufficient.
  • the content exceeds 5% by weight, the transparency of the film is insufficient. There is a case.
  • the method of blending particles in the film is not particularly limited, and a conventionally known method can be adopted.
  • it can be added at any stage of producing the polyester, but it is preferably added after completion of the esterification or transesterification reaction.
  • 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 is done by methods.
  • antioxidants In addition to the above-mentioned particles, conventionally known antioxidants, antistatic agents, heat stabilizers, lubricants, dyes, pigments and the like can be added to the film as necessary.
  • the thickness of the polyester film is not particularly limited as long as it can be formed as a film, but is usually 10 to 350 ⁇ m, preferably 38 to 125 ⁇ m, and more preferably 50 to 100 ⁇ m. If the film thickness is less than 10 ⁇ m, external foreign matter generated in the process etc. will be transferred to the adhesive when processing the adhesive sheet in this application, and the coatability is poor during the release film processing. There are problems such as deteriorating productivity. When the film thickness is thick, a costly problem arises.
  • a production example of the polyester film will be specifically described, but is not limited to the following production example. 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.
  • the film is stretched in the direction perpendicular to the first stretching direction.
  • the stretching temperature is usually 90 to 170 ° C.
  • the stretching ratio is usually 3.0 to 7 times, preferably 3.5 to 6 times. is there.
  • heat treatment is performed at a temperature of 180 to 270 ° C. under tension or relaxation within 30% to obtain a biaxially oriented film.
  • 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.
  • a simultaneous biaxial stretching method is a method in which the above-mentioned unstretched sheet is stretched and oriented in the machine direction and the width direction at a temperature controlled usually at 90 to 140 ° C., preferably 80 to 110 ° C. Is an area magnification of 4 to 50 times, preferably 7 to 35 times, and more preferably 10 to 25 times. 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.
  • a conventionally known stretching method such as a screw method, a pantograph method, or a linear driving method can be employed.
  • the coating layer obtained by applying a coating solution containing polyvinyl alcohol>
  • the coating layer is provided to prevent process contamination due to OL and contamination when bonded to the pressure-sensitive adhesive layer.
  • the content of polyvinyl alcohol in the coating layer is usually 10 to 100% by weight, preferably 20 to 90% by weight, more preferably 30 to 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.
  • Polyvinyl alcohol 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 saponification degree of polyvinyl alcohol is not particularly limited, but is usually 70 mol% or more, preferably 80 mol% or more and 99.9 mol% or less.
  • Binder resin is a polymer compound safety evaluation flow scheme (November 1985, sponsored by the Chemical Substances Council) with a high number average molecular weight (Mn) of 1000 or more by gel permeation chromatography (GPC) measurement. It can be defined as a molecular compound having film-forming properties.
  • 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.
  • binder resin having a composite structure examples 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.
  • the coating layer may contain a crosslinking reactive compound as required.
  • Cross-linking reactive compounds include methylolated or alkylolized urea-based, melamine-based, guanamine-based, acrylamide-based, polyamide-based compounds, polyamines, epoxy compounds, oxazoline compounds, aziridine compounds, blocked isocyanate compounds, silane cups
  • Polyfunctional low molecular 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.
  • the crosslinking reactive compound can improve the cohesiveness, surface hardness, scratch resistance, solvent resistance, and water resistance of the coating layer by crosslinking reaction with the functional group of the resin contained in the coating layer.
  • 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
  • the functional group of the easily adhesive polyester is an organic acid or an anhydride thereof.
  • epoxy-based compounds, melamine-based compounds, oxazoline-based compounds, metal chelates and the like are preferable as the cross-linking reactive compound.
  • the functional group of the easy-adhesion resin is an amine
  • an epoxy-based compound is 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.
  • the melamine compound include methoxymethyl melamine and butoxymethylated melamine which are alkylol or alkoxyalkylol 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 always contains two or more functional groups in one molecule.
  • the blending 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 coating layer.
  • the coating layer forms a barrier layer densely, so that OL can be more effectively suppressed. 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.
  • the coating layer may contain inert particles for improving the slipperiness of the coating layer as necessary.
  • the inert particles include inorganic inert particles and organic inert particles.
  • the inorganic inert particles include silica sol, alumina sol, calcium carbonate, and titanium oxide.
  • 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 has a relationship of 1/3 ⁇ d / L ⁇ 3, and further 1/2 ⁇ d / L ⁇ 2, when the average film thickness of the coating layer is (L). It is preferable to select so as to satisfy.
  • the coating layer is a surfactant, antifoaming agent, coating property improver, thickener, low molecular antistatic agent, organic lubricant, antioxidant, ultraviolet absorber, foaming agent, dye, pigment as necessary
  • a small amount of such additives may be contained. These additives may be used alone or in combination of two or more as necessary.
  • the coating layer 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.
  • 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
  • the coating solution used for forming the coating layer is usually preferably adjusted with water as the main medium from the viewpoint of safety and hygiene.
  • water is the main medium
  • a small amount of an organic solvent may be contained for the purpose of improving the dispersion in water or improving the film forming performance.
  • the organic solvent is preferably used as long as it is dissolved in water when mixed with water, which is the main medium. However, if it is a stable emulsion (emulsion) that does not separate after standing for a long time, Alternatively, it may be used in a state where it does not dissolve in water.
  • the organic solvent may be used alone or in combination of two or more as necessary.
  • the method of providing the coating layer is not particularly limited, but a method of applying a coating solution (in-line coating) in the process of manufacturing the polyester film is suitably employed. Specifically, a method of applying and drying a coating solution on the surface of an unstretched sheet, a method of applying and drying a coating solution on the surface of a uniaxially stretched film, and a method of applying and drying a coating solution on the surface of a biaxially stretched film Etc. Among these, it is economical to apply a coating solution on the surface of an unstretched film or a uniaxially stretched film, and then simultaneously dry and cure the coating layer in the process of heat-treating the film.
  • a method for forming the coating layer a method in which some of the above-described coating methods are used in combination can be adopted as necessary. Specifically, a method of applying a first layer on the surface of an unstretched sheet and drying, then stretching in a uniaxial direction, and then applying and drying a second layer can be used.
  • a coating layer When providing a coating layer by in-line coating, apply the above-mentioned series of compounds as an aqueous solution or water dispersion on a polyester film with a coating solution adjusted to a solid content concentration of about 0.1 to 50% by weight. 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.
  • the drying and curing conditions for forming the coating layer on the polyester film are not particularly limited.
  • the standard is usually 70 to 280 ° C. for 3 to 200 seconds. It is better to perform heat treatment.
  • the polyester film may be subjected to surface treatment such as corona treatment or plasma treatment in advance.
  • the amount of OL extracted from the coating layer surface with dimethylformamide after heat treatment is 1.0 mg / m 2 or less. Preferably there is.
  • OL exceeds 1.0 mg / m 2 , there is a process contamination, and when the adhesive is bonded, a foreign matter may be generated, resulting in a problem such as a decrease in product yield.
  • the thickness of the coating layer is usually in the range of 0.002 to 1.0 g / m 2 , preferably 0.005 to 0.5 g / m 2 , more preferably 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. Analysis of the components in the coating layer can be performed by surface analysis such as TOF-SIMS.
  • a film having a structure in which a polyester having a low OL content is coextruded and laminated on at least one surface of a layer composed of a polyester having a normal OL content may be used.
  • the effect of preventing bright spots due to the precipitated OL is obtained, which is particularly preferable.
  • the release layer in the present invention comprises a silicone resin (a) having an alkenyl group as a functional group, a silicone resin (b) having an alkyl group as a functional group, a migration component (c) to the adhesive layer, and a platinum catalyst ( It is a silicone release layer containing d).
  • 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 / methyl-blocked dimethylhexenylsiloxy group blocked at both ends of the molecular chain Hexenylsiloxane copolymer (95 mol% of dimethylsiloxane units, 5 mol% of methylhexenylsiloxane units).
  • the curable silicone resin containing an alkyl group is a trimethylsiloxy group-blocked methylhydrogenpolysiloxane having both molecular chains and trimethylsiloxy group-blocked dimethylsiloxane / methylhydrogensiloxane as both organohydrogenpolysiloxanes.
  • examples thereof include a polymer, a dimethylhydrogensiloxy group-capped methylhydrogen polysiloxane having both molecular chains, and a dimethylsiloxane / methylhydrogensiloxane copolymer having both molecular chains having both ends dimethylhydrogensiloxy group-capped.
  • the release film of the present invention is used by sticking the release layer to the adhesive layer of the base-less double-sided pressure-sensitive adhesive sheet, but the above-mentioned silicone resin contains a component that migrates to the adhesive layer.
  • Silicone oil is typically used as the migration component.
  • the silicone oil is a silicone oil called straight silicone oil or modified silicone oil, and examples thereof include the following. Examples of the straight silicone include dimethyl silicone oil, methylphenyl silicone oil, methyl hydrogen silicone oil, and the like.
  • modified silicone oil side chain type polyether modified, aralkyl modified, fluoroalkyl modified, long chain alkyl modified, higher fatty acid ester modified, higher fatty acid amide modified, polyether / long chain alkyl modified / aralkyl modified, Examples include phenyl modification, polyether modification at both ends, and polyether / methoxy modification. Both straight silicone oil and modified silicone oil are non-reactive, non-functional oils.
  • the content of the migration component is 5 to 20% by weight, preferably 10 to 13% by weight, more preferably 0.1 to 5.0% by weight.
  • the content of the transition component is lower than 5%, the speed dependency described later is increased, and when it exceeds 20% by weight, the curability is remarkably lowered and the adhesion is deteriorated.
  • silicone-based resin coatings that can be used in the present invention include KS-774, KS-775, KS-778, KS-779H, KS-847H, KS-856, X, manufactured by Shin-Etsu Chemical Co., Ltd. -62-2422, X-62-2461; DKQ3-202, DKQ3-203, DKQ3-204, DKQ3-205, DKQ3-210 manufactured by Dow Corning Asia Ltd .; YSR- manufactured by Toshiba Silicone Corp.
  • a release control agent may be used in combination to adjust the release property of the release layer.
  • the silicone-based resin coating material is composed of a silicone resin (a) having an alkenyl group as a functional group, a silicone resin (b) having an alkyl group as a functional group, and a component (c) for transferring to an adhesive layer.
  • the ratio of the silicone resin having an alkenyl group as (a) and the silicone resin having an alkyl group as a functional group (b) is (b) / (a) is usually 0.5 to 2 weight ratio.
  • a silicone resin having an alkenyl group and an alkyl group as a functional group may be used.
  • a conventionally known coating method can be used as in the case of the above-mentioned coating layer.
  • the coating amount when forming the release layer is usually in the range of 0.01 to 1 g / m 2 .
  • 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 is subjected to a surface treatment such as corona treatment or plasma treatment. May be.
  • a platinum-based catalyst that promotes an addition-type reaction is used in order to make the release layer clean and robust.
  • 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 release layer is usually 0.3 to 3.0% by weight, preferably 0.5 to 2.0% by weight.
  • the platinum-based catalyst content in the release layer is lower than 0.3% by weight, there may be problems such as deterioration of the surface condition due to insufficient peeling force and insufficient curing reaction in the coating layer.
  • the platinum-based catalyst content in the release layer exceeds 3.0% by weight, the cost is increased, and the process becomes defective due to increased reactivity and generation of gel foreign matter. Sometimes.
  • the component is an organic compound having a carbon-carbon triple bond and a hydroxyl group, preferably 3-methyl-1-butyn-3-ol, 3,5-dimethyl-1-hexyn-3-ol and phenyl. It is a compound selected from the group consisting of butinol.
  • 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 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, It is preferable to change according to the desired peeling force. 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 residual adhesion rate with 31B tape is usually 65% to 90%, preferably 70% to 85%.
  • the residual adhesion rate is lower than 65%, the transferability is high, and the adhesive moves to roll dirt or the adhesive surface during the adhesive processing, resulting in a decrease in adhesive peeling force. Further, when the residual adhesion rate is 90% or more, the speed dependency cannot be reduced.
  • the value of the peel force of the release film of the present invention is such that the low speed peel force in the range of 300 mm / min is 10 to 20 mN / cm.
  • 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 off.
  • the peel force exceeds 20 mN / cm, the difference in peel force between the release film with the greater peel force will be small, causing problems in the peel process, and the selection range for the release film with the greater peel force will be narrow. There are problems such as becoming.
  • the high speed peeling force in the 10,000 mm / min speed region taking into consideration workability is 2.5 times or less of the above low speed peeling force. If the peel force ratio is larger 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 may be peeled off. To do.
  • Martens hardness of the release layer of the release film of the present invention is usually 400 N / mm 2 or more, preferably, 450 N / mm 2 or more.
  • the Martens hardness of the release layer is less than 400 N / mm 2 , the release film dependency of the release film increases, and the film surface is easily damaged and OL is likely to occur. May occur.
  • the above-mentioned Martens hardness means a hardness obtained by an instrumented indentation hardness test on a surface layer using a hardness measuring machine using a triangular pyramid indenter, and a test of 115 ° triangular pyramid indenter and 0.10 mN. It is a value measured by force.
  • foreign matter or light interference color may be generated in the optical inspection of the process depending on the application.
  • a means for satisfying the range of the MOR_C value of the polyester film is to appropriately select the stretching conditions for the desired film thickness during film formation.
  • the MOR_C value of the polyester film is usually 1.5 to 3.0, preferably 1.8 to 2.7, more preferably 2.1 to 2.4.
  • the MOR_C value is larger than 3.0, the release layer is not uniform, and in the case where there is an optical inspection, problems such as easy appearance of the light interference color may occur.
  • the MOR_C value is smaller than 1.5, there is a problem that the production yield of the release film itself is deteriorated.
  • the polyester film is sampled at an arbitrary length L (cm) in the longitudinal direction (hereinafter abbreviated as MD) and the lateral width direction (hereinafter abbreviated as TD). 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.
  • Transferability evaluation adhesion rate of release film The sample film was cut to A4 size, and 75 ⁇ m thick biaxially stretched PET film (Mitsubishi Chemical Polyester Film Co., Ltd .: Diafoil T100-75) was layered on the release surface and pressed for 2 hours under the conditions of temperature 60 ° C and pressure 1MPa. To do. A 75 ⁇ m-thick film pressed against this release surface is used as a migration evaluation film. Similarly, a 75 ⁇ m-thick biaxially stretched PET film (same as above) is pressed against an untreated PET film as a reference film. Adhesive tape (“No.
  • Transferability evaluation adhesion rate (%) (Peeling force of transferability evaluation film ⁇ Peeling force of reference film) ⁇ 100 In a film having a high migration property, since a lot of silicone adheres to the pressed film, the peeling force of the adhesive tape is reduced, and the migration evaluation adhesion rate (%) is also lowered.
  • X Less than 10 mN / cm or more than 20 mN / cm.
  • Mold 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. (Triangle
  • the recovered DMF was supplied to a liquid chromatography (manufactured by Shimadzu Corporation: LC-7A) to determine the amount of OL in DMF, and this value was divided by the film area in contact with DMF to obtain the amount of OL on the film surface (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 temperature: 40 ° C Flow rate: 1 ml / min Detection wavelength: 254 nm
  • MOR_C value measurement of polyester film by microwave molecular orientation meter The MOR_C value was determined from the transmission microwave intensity pattern using a microwave molecular orientation meter manufactured by Oji Scientific Instruments.
  • MOR_C value measurement of polyester film by microwave molecular orientation meter The MOR_C value was determined from the transmission microwave intensity pattern using a microwave molecular orientation meter manufactured by Oji Scientific Instruments. Judgment is based on the following criteria. ⁇ : The range is from 2.0 to 2.5. ⁇ : The range is 1.5 to 1.9 or 2.6 to 3.0. X: It is lower than 1.5% or higher than 3.0.
  • the width direction of the release film obtained by applying a release agent on the film and having a dryer temperature of 120 ° C. and a line speed of 30 m / min is parallel to the alignment axis of the polarizing film.
  • the release film was adhered to the polarizing film through the pressure-sensitive adhesive to obtain a polarizing plate.
  • black metal powder (foreign matter) having a size of 50 ⁇ m or more was mixed between the pressure-sensitive adhesive and the polarizing film so as to be 50 / m 2 .
  • a polarizing plate for inspection is superimposed on the polarizing plate release film mixed with the foreign matter thus obtained so that the orientation axis is orthogonal to the width direction of the release film, and white light is irradiated from the polarizing plate side. Then, it was visually observed from a polarizing plate for inspection, and whether or not a foreign matter mixed between the adhesive and the polarizing film was found under crossed Nicols was evaluated according to the following criteria.
  • A4 size samples were cut out from a total of three locations in the center and both ends in the width direction of the obtained film.
  • Foreign matter can be recognized with relatively no problem.
  • X Foreign matter recognition is poor.
  • ⁇ and ⁇ are the levels where there is no problem in actual use. Among the above criteria, those above ⁇ are levels that can be used without any problem in actual use.
  • 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.
  • 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.
  • 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.
  • the pressure was gradually reduced from normal pressure, and finally 0.3 mmHg.
  • 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.
  • 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.
  • 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.
  • the film was stretched 2.8 times in the longitudinal direction at 100 ° C., then subjected to a preheating step in a tenter and subjected to a transverse stretching of 5.1 times at 120 ° C., followed by heat treatment at 220 ° C. for 10 seconds, 4% relaxation was added in the width direction at 180 ° C. 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 50 ⁇ m (layer structure: surface layer 2.5 ⁇ m / intermediate layer 45 ⁇ m / surface layer 2.5 ⁇ m).
  • a release agent composed of release agent composition-A shown below was applied to the obtained polyester film by a reverse gravure coating method so that the coating amount (after drying) was 0.12 g / m 2 , and a dryer temperature of 120 A roll-shaped release polyester film was obtained under the conditions of ° C and a line speed of 30 m / min.
  • the obtained release polyester film had a release force of 14 mN / cm at a speed of 300 mm / min and a release force of 32 mN / cm at a speed of 10,000 mm / min.
  • a deflector plate was prepared by the following method, and optical property inspection and peeling properties were evaluated.
  • the obtained release film had good inspection by reflection and good recognition of foreign matter, and the polarizing plate was peeled off cleanly, and the phenomenon that the adhesive adhered to the release layer was not observed.
  • polarizing plate with release film The acrylic adhesive shown below is applied to the polarizing plate so that the thickness after drying is 25 ⁇ m, and after passing through a 130 ° C. drying oven in 30 seconds, the release film is bonded, and the adhesive is interposed.
  • 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
  • Example 2 In Example 1, the draw ratio at the time of manufacturing the polyester film, the coating thickness that changes the film thickness, the coating amount containing polyvinyl alcohol, the coating amount of the silicone release layer (after drying), and the amount of the migration component of the release agent composition A polyester film was obtained in the same manner as in Example 1 except that the above was changed. The obtained results are summarized in Table 1 below.
  • Comparative Example 1 A polyester film was obtained in the same manner as in Example 1 except that the release agent composition was changed as follows. The results obtained are summarized in Table 2 below.
  • Comparative Example 2 A polyester film was obtained in the same manner as in Example 1 except that the release agent composition was changed as follows. The results obtained are summarized in Table 2 below.
  • Comparative Example 3 A polyester film was obtained in the same manner as in Example 1 except that ⁇ mold release composition-A> and the coating amount was changed to 0.25 g / m 2 . The results obtained are summarized in Table 2 below.
  • Comparative Example 4 A polyester film was obtained in the same manner as in Comparative Example 1 except that ⁇ Release Composition-C> in Comparative Example 1 and the coating amount was changed to 0.08 g / m 2 . The results obtained are summarized in Table 2 below.
  • Example 1 it changes like the film thickness at the time of polyester film manufacture, It changes like Example 1 except changing the application quantity (after drying) of the coating layer containing polyvinyl alcohol, and a silicone type release layer. Manufactured to obtain a polyester film. The obtained results are summarized in Table 3 below.
  • Comparative Example 10 A polyester film was obtained in the same manner as in Example 2 except that the release agent composition A was added with 3 parts of silicone oil (AL-1). The obtained results are summarized in Table 3 below.

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Abstract

Provided is an inexpensive mold release film, whereby it becomes possible to minimize the peel rate dependency when a base-less double-sided adhesive sheet is used for optical purposes, for example in a touch panel, a liquid crystal polarizing plate and a retardation plate, to improve the productivity, cost performance or the like of the mold release film, and to impart a property of preventing the formation of any oligomer or a property of testing on the formation of any oligomer to the mold release film to thereby reduce the occurrence of contamination during a process or the formation of foreign substances in an adhesive agent. A mold release film comprising a polyester film having a mold release layer, wherein the mold release layer is bonded to an adhesive layer in a base-less double-sided adhesive sheet upon use, the mold release layer is a silicone-type mold release layer comprising (a) a silicone resin having an alkenyl group as a functional group, (b) a silicone resin having an alkyl group as a functional group, (c) a component capable of migrating into the adhesive layer, and (d) a platinum-containing catalyst, the content of the component (c) capable of migrating is 5-20 wt%, the low-speed peel force of the mold release layer at a speed of 300 mm/min falls within the range of 10-20 mN/cm, and the high-speed peel force of the mold release layer at a speed of 10000 mm/min is up to 2.5 times greater than the low-speed peel force.

Description

離型フィルムRelease film

 本発明は、離型フィルムに関し、詳しくは、光学用途向けとして好適な基材レス両面粘着シート用に使用される離型フィルム関するものである。 The present invention relates to a release film, and more particularly to a release film used for a substrate-less double-sided pressure-sensitive adhesive sheet suitable for optical applications.

 従来、物体間を面接着する粘着シートは種々知られており、粘着シートの1つとして基材レス両面粘着シートが知られている。基材レス両面粘着シートは、粘着剤層の両面に剥離力の相対的に低い軽剥離シートと、剥離力の相対的に高い重剥離シートが積層されて構成され、両面の剥離シートを除去した後には、支持基材を有さない粘着剤層のみとなる両面粘着シートである。基材レス両面粘着シートは、まず軽剥離シートが剥がされ、露出された粘着剤層の一方の面が物体面に接着され、その接着後、さらに重剥離シートが剥がされ、露出された粘着剤層の他方の面が、異なる物体面に接着され、これにより物体間が面接着される。 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.

 近年、基材レス両面粘着シートは、その用途が広がりつつあり、各種光学用途の部材等にも用いられている。例えば、LCDの部材として、基材レス両面粘着剤シートの剥離力の軽い方の離型フィルムを剥がして、その面に偏光板を貼り合わせて、その反対面側に剥離力の重い離型フィルムを用いることがある。 In recent years, the baseless double-sided pressure-sensitive adhesive sheet has been used for various optical applications and the like. 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.

 生産上の作業性から、ある程度高速域での加工が考えられるが、軽剥離の離型フィルムにおいて、軽い剥離力を達成するのはもちろんだが、それを達成しつつ、加工速度を上げても、できるだけ重剥離の離型フィルムとの剥離力差が縮まらないことを同時に達成することは非常に難しい(特許文献1)。もし、重剥離の離型フィルムとの剥離力差が縮まったならば、剥離工程において、両面のフィルムが同時に剥がれる、また、剥離力差が小さくなるために粘着剤も一緒に剥がれる等の問題が起こり、加工性、生産性に不具合をきたすことになる(特許文献2)。 In terms of workability in production, processing in a high speed range can be considered to some extent, but in the release film of light release, of course, to achieve a light release force, It is very difficult to simultaneously achieve that the difference in peel force from the release film that is as heavy as possible is not reduced (Patent Document 1). 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 (Patent Document 2).

 上記の剥離力差の制御は非常に難しく、シリコーン成分の種々選択とコントロールが必要であり(特許文献1及び2)、しかも、シリコーン塗布膜の硬さのコントロールも必要であると考えられる。 It is very difficult to control the above difference in peeling force, and various selection and control of the silicone component are necessary (Patent Documents 1 and 2), and it is also considered necessary to control the hardness of the silicone coating film.

 また、基材レス両面粘着シートにおいて、タッチパネルやモニターの比較的面積の小さなフラットパネルなどの外側に使用される用途では、製品にした時に人の目が近く、異物などの輝点が目立つと視覚的に不具合が生じるために、検査を強化する場合がある。このとき、基材レス両面粘着シートに離型フィルムを貼り合わせたままの検査が行なわれることもある。その場合、フィルムの異物が少ないものは当然として、検査容易化のために、フィルムの光軸、つまり、分子の配向を管理する必要性が出てくる(特許文献3)。 Also, in applications that are used on the outside of a flat panel with a relatively small area, such as a touch panel and a monitor, in a baseless double-sided pressure-sensitive adhesive sheet, human eyes are close when the product is used, and if bright spots such as foreign objects are noticeable, it is visually In some cases, the inspection may be strengthened due to problems. At this time, the inspection may be performed while the release film is bonded to the baseless double-sided pressure-sensitive adhesive sheet. In that case, as a matter of course, it is necessary to manage the optical axis of the film, that is, the orientation of the molecule for the purpose of facilitating inspection (Patent Document 3).

 さらに、上記に述べた異物の1つには、ポリエステルフィルム起因のオリゴマーといわれる低分子成分が起因することがある。このオリゴマーを防ぐことができたならば、上記の生産時の異物不具合を押さえることができ、かつ、フィルム、および、その先の工程汚染を防ぐ事ができる。なお、本発明おいて、オリゴマー(OL)とは、熱処理後、結晶化してフィルム表面に析出する低分子量物のうちの環状三量体と定義する。 Furthermore, one of the foreign substances described above may be caused by a low molecular component called an oligomer derived from a polyester film. If this oligomer can be prevented, the above-mentioned foreign matter malfunction during production can be suppressed, and the film and the subsequent process contamination can be prevented. In the present invention, the oligomer (OL) is defined as a cyclic trimer among low molecular weight substances that crystallize after heat treatment and precipitate on the film surface.

特開2009-220496号公報JP 2009-220696 A 特開平10-158519号公報Japanese Patent Laid-Open No. 10-158519 特開2003-231214号公報JP 2003-231214 A

 本発明は、上記実情に鑑みなされたものであって、その解決課題は、基材レス両面粘着シートを光学用途、例えば、タッチパネル、液晶偏向板、位相差板等において使用する際、剥離速度依存性を最小限に抑えることを可能にし、生産性、コストなどの問題を解決し、かつ、オリゴマーを防止性、検査性を付与することで、工程汚染や粘着剤への異物軽減を図った、安価な離型フィルムを提供することにある。 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 depends on the peeling rate when used in optical applications, for example, touch panels, liquid crystal deflecting plates, retardation plates, and the like. It is possible to minimize productivity, solve problems such as productivity, cost, etc., and provide oligomers with preventability and inspection properties, thereby reducing process contamination and foreign substances to adhesives. The object is to provide an inexpensive release film.

 本発明者は、上記実情に鑑み鋭意検討した結果、特定の構成の離型層を有するポリエステルフィルムによれば、上記課題を容易に解決できることを見いだし、本発明を完成するに至った。 As a result of intensive studies in view of the above circumstances, the present inventor has found that the above problem can be easily solved by a polyester film having a release layer having a specific configuration, and has completed the present invention.

 すなわち、本発明の要旨は、離型層を備えたポリエステルフィルムから成り、離型層を基材レス両面粘着シートの粘着層に張り合わせて使用される離型フィルムであり、離型層が、官能基としてアルケニル基を有するシリコーン樹脂(a)、アルキル基を有するシリコーン樹脂(b)、粘着層への移行成分(c)、及び、白金系触媒(d)を含有し、移行成分(c)の含有量が5~20重量%であるシリコーン系離型層であり、離型層の300mm/分速度域での低速剥離力が10~20mN/cmの範囲であり、かつ、10000mm/分速度域での高速剥離力が低速剥離力の2.5倍以下であることを特徴とする離型フィルムに存する。 That is, the gist of the present invention is a release film composed of a polyester film provided with a release layer, which is used by laminating the release layer to the adhesive layer of the base-less double-sided pressure-sensitive adhesive sheet. A silicone resin (a) having an alkenyl group as a group, a silicone resin (b) having an alkyl group, a migration component (c) to the adhesive layer, and a platinum-based catalyst (d), and containing the migration component (c) It is a silicone-based release layer having a content of 5 to 20% by weight, and the release layer has a low-speed peeling force in the range of 300 mm / min at a speed range of 10 to 20 mN / cm, and a speed range of 10,000 mm / min. The release film is characterized in that the high-speed peeling force is 2.5 times or less of the low-speed peeling force.

 そして、本発明の好ましい態様の層構成においては、ポリエステルフィルムとシリコーン系離型層との間にポリビニルアルコールを含有する塗布液を塗布して得られた塗布層を有する。 And in the layer structure of the preferable aspect of this invention, it has a coating layer obtained by apply | coating the coating liquid containing polyvinyl alcohol between a polyester film and a silicone type release layer.

 本発明によれば、軽剥離で剥離速度依存性が小さい離型フィルムを提供することができるため、その工業的価値は高い。 According to the present invention, it is possible to provide a release film that is lightly peeled and has a small peel rate dependency, and therefore has high industrial value.

<ポリエステルフィルム>
 本発明の離型フィルムの基材であるポリエステルフィルムとは、いわゆる押出法に従い押出口金から溶融押出されたシートを延伸したフィルムである。
<Polyester film>
The polyester film which is the base material of the release film of the present invention is a film obtained by stretching a sheet melt-extruded from an extrusion die according to a so-called extrusion method.

 上記のフィルムを構成するポリエステルとは、ジカルボン酸と、ジオールとからあるいはヒドロキシカルボン酸から重縮合によって得られるエステル基を含むポリマーを指す。
 ジカルボン酸としては、テレフタル酸、イソフタル酸、アジピン酸、アゼライン酸、セバシン酸、2,6-ナフタレンジカルボン酸、1,4-シクロヘキサンジカルボン酸等を、ジオールとしては、エチレングリコール、1,4-ブタンジオール、ジエチレングリコール、トリエチレングリコール、ネオペンチルグリコール、1,4-シクロヘキサンジメタノール、ポリエチレングリコール等を、ヒドロキシカルボン酸としては、p-ヒドロキシ安息香酸、6-ヒドロキシ-2-ナフトエ酸等をそれぞれ例示することができる。かかるポリマーの代表的なものとして、ポリエチレンテレフタレートやポリエチレン-2、6-ナフタレート等が例示される。
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.
Dicarboxylic acids include terephthalic acid, isophthalic acid, adipic acid, azelaic acid, sebacic acid, 2,6-naphthalenedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, etc., and diols include ethylene glycol, 1,4-butane. Examples include diol, diethylene glycol, triethylene glycol, neopentyl glycol, 1,4-cyclohexanedimethanol, and polyethylene glycol. Examples of hydroxycarboxylic acid include p-hydroxybenzoic acid and 6-hydroxy-2-naphthoic acid. be able to. Typical examples of such polymers include polyethylene terephthalate and polyethylene-2,6-naphthalate.

 フィルム中には、易滑性の付与および各工程での傷発生防止を主たる目的として、粒子を配合することが好ましい。配合する粒子の種類は、易滑性付与可能な粒子であれば特に限定されるものではなく、具体例としては、例えば、シリカ、炭酸カルシウム、炭酸マグネシウム、炭酸バリウム、硫酸カルシウム、リン酸カルシウム、リン酸マグネシウム、カオリン、酸化アルミニウム、酸化チタン等の粒子が挙げられる。また、特公昭59-5216号公報、特開昭59-217755号公報等に記載されているような耐熱性有機粒子を用いてもよい。この他の耐熱性有機粒子の例として、熱硬化性尿素樹脂、熱硬化性フェノール樹脂、熱硬化性エポキシ樹脂、ベンゾグアナミン樹脂等が挙げられる。さらに、ポリエステル製造工程中、触媒等の金属化合物の一部を沈殿、微分散させた析出粒子を用いることもできる。 In the film, it is preferable to incorporate particles mainly for the purpose of imparting slipperiness and preventing 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.

 一方、粒子の形状に関しても特に限定されるわけではなく、球状、塊状、棒状、扁平状等のいずれを用いてもよい。また、その硬度、比重、色等についても特に制限はない。これら一連の粒子は、必要に応じて2種類以上を併用してもよい。 On the other hand, the shape of the particles 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 also about the hardness, specific gravity, a color, etc. These series of particles may be used in combination of two or more as required.

 また、粒子の平均粒径は、通常0.01~3μm、好ましくは0.1~2μmの範囲である。平均粒径が0.01μm未満の場合には、易滑性を十分に付与できない場合がある。一方、3μmを超える場合には、フィルムの製膜時に、その粒子の凝集物のために透明性が低下することがある他に、破断などを起こし易くなり、生産性の面で問題になることがある。 The average particle diameter of the particles is usually in the range of 0.01 to 3 μm, preferably 0.1 to 2 μm. 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.

 さらに粒子含有量は、通常0.001~5重量%、好ましくは0.005~3重量%の範囲である。粒子含有量が0.001重量%未満の場合には、フィルムの易滑性が不十分な場合があり、一方、5重量%を超えて添加する場合には、フィルムの透明性が不十分な場合がある。 Further, the particle content 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.

 フィルム中に粒子を配合する方法としては、特に限定されるものではなく、従来公知の方法を採用しうる。例えば、ポリエステルを製造する任意の段階において添加することができるが、好ましくはエステル化もしくはエステル交換反応終了後、添加するのが良い。 The method of blending particles in the film is not particularly limited, and a conventionally known method can be adopted. For example, it can be added at any stage of producing the polyester, but it is preferably added after completion of the esterification or transesterification reaction.

 また、ベント付き混練押出機を用い、エチレングリコールまたは水などに分散させた粒子のスラリーとポリエステル原料とをブレンドする方法、または、混練押出機を用い、乾燥させた粒子とポリエステル原料とをブレンドする方法などによって行われる。 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.

 なお、フィルム中には、上述の粒子以外に必要に応じて従来公知の酸化防止剤、帯電防止剤、熱安定剤、潤滑剤、染料、顔料等を添加することができる。 In addition to the above-mentioned particles, conventionally known antioxidants, antistatic agents, heat stabilizers, lubricants, dyes, pigments and the like can be added to the film as necessary.

 ポリエステルフィルムの厚みは、フィルムとして製膜可能な範囲であれば特に限定されるものではないが、通常10~350μm、好ましくは38~125μm、更に好ましくは、50~100μmの範囲である。フィルム厚みが10μmより薄い場合、本用途で粘着剤シートを加工するときに工程等で発生した外部異物を粘着剤に転写させてしまう、また、離型フィルム加工の際に、塗工性が悪く、生産性を悪化させてしまう、等の問題が挙げられる。フィルム厚みが厚い場合、コストがかかる不具合が生じる。 The thickness of the polyester film is not particularly limited as long as it can be formed as a film, but is usually 10 to 350 μm, preferably 38 to 125 μm, and more preferably 50 to 100 μm. If the film thickness is less than 10 μm, external foreign matter generated in the process etc. will be transferred to the adhesive when processing the adhesive sheet in this application, and the coatability is poor during the release film processing. There are problems such as deteriorating productivity. When the film thickness is thick, a costly problem arises.

 次に、ポリエステルフィルムの製造例について具体的に説明するが、以下の製造例に何ら限定されるものではない。すなわち、先に述べたポリエステル原料を使用し、ダイから押し出された溶融シートを冷却ロールで冷却固化して未延伸シートを得る方法が好ましい。この場合、シートの平面性を向上させるためシートと回転冷却ドラムとの密着性を高めることが好ましく、静電印加密着法および/または液体塗布密着法が好ましく採用される。次に得られた未延伸シートは二軸方向に延伸される。その場合、まず、前記の未延伸シートを一方向にロールまたはテンター方式の延伸機により延伸する。延伸温度は、通常90~140℃、好ましくは95~120℃であり、延伸倍率は通常2.5~7倍、好ましくは3.0~6倍である。次いで、一段目の延伸方向と直交する方向に延伸するが、その場合、延伸温度は通常90~170℃であり、延伸倍率は通常3.0~7倍、好ましくは3.5~6倍である。そして、引き続き180~270℃の温度で緊張下または30%以内の弛緩下で熱処理を行い、二軸配向フィルムを得る。上記の延伸においては、一方向の延伸を2段階以上で行う方法を採用することもできる。その場合、最終的に二方向の延伸倍率がそれぞれ上記範囲となるように行うのが好ましい。 Next, a production example of the polyester film will be specifically described, but is not limited to the following production example. 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 this 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 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.

 また、ポリエステルフィルム製造に関しては、同時二軸延伸法を採用することもできる。同時二軸延伸法は、前記の未延伸シートを通常90~140℃、好ましくは80~110℃で温度コントロールされた状態で機械方向および幅方向に同時に延伸し配向させる方法であり、延伸倍率としては、面積倍率で4~50倍、好ましくは7~35倍、更に好ましくは10~25倍である。そして、引き続き、170~250℃の温度で緊張下または30%以内の弛緩下で熱処理を行い、延伸配向フィルムを得る。上述の延伸方式を採用する同時二軸延伸装置に関しては、スクリュー方式、パンタグラフ方式、リニアー駆動方式等、従来公知の延伸方式を採用することができる。 Also, for the production of a polyester film, a simultaneous biaxial stretching method can be employed. The simultaneous biaxial stretching method is a method in which the above-mentioned unstretched sheet is stretched and oriented in the machine direction and the width direction at a temperature controlled usually at 90 to 140 ° C., preferably 80 to 110 ° C. Is an area magnification of 4 to 50 times, preferably 7 to 35 times, and more preferably 10 to 25 times. 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.

<ポリビニルアルコールを含有する塗布液を塗布して得られた塗布層>
 上記の塗布層は、OL封止目的の他、OLによる工程汚染、また、粘着剤層へ貼り合せる際の汚染を防ぐために設けられる。
<Coating layer obtained by applying a coating solution containing polyvinyl alcohol>
In addition to the purpose of OL sealing, the coating layer is provided to prevent process contamination due to OL and contamination when bonded to the pressure-sensitive adhesive layer.

 塗布層におけるポリビニルアルコールの含有量は、通常10~100重量%、好ましくは20~90重量%、更に好ましくは30~90重量%である。ポリビニルアルコールの含有量が10重量%未満では、オリゴマー封止効果が不十分で好ましくない。 The content of polyvinyl alcohol in the coating layer is usually 10 to 100% by weight, preferably 20 to 90% by weight, more preferably 30 to 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.

 ポリビニルアルコールは、通常の重合反応によって合成することができ、水溶性であることが好ましい。ポリビニルアルコールの重合度は、特に限定されるものではないが、通常100以上、好ましくは300~40000である。重合度が100以下の場合、塗布層の耐水性が低下する傾向がある。ポリビニルアルコールのけん化度は、特に限定されるものではないが、通常70モル%以上、好ましくは80モル%以上、99.9モル%以下である。 Polyvinyl alcohol 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 saponification degree of polyvinyl alcohol is not particularly limited, but is usually 70 mol% or more, preferably 80 mol% or more and 99.9 mol% or less.

 塗布層には、必要に応じて上記のポリビニルアルコール以外の水溶性または水分散性のバインダー樹脂を併用してもよい。バインダー樹脂とは、高分子化合物安全性評価フロースキーム(昭和60年11月 化学物質審議会主催)に準じて、ゲルパーミエーションクロマトグラフィー(GPC)測定による数平均分子量(Mn)が1000以上の高分子化合物で、かつ造膜性を有するものと定義することができる。かかるバインダー樹脂としては、例えば、ポリエステル、ポリウレタン、アクリル樹脂、ビニル樹脂、エポキシ樹脂、アミド樹脂、アクリレート樹脂、等が挙げられる。これらは、それぞれの骨格構造が共重合等により実質的に複合構造を有していてもよい。複合構造を持つバインダー樹脂としては、例えば、アクリル樹脂グラフトポリエステル、アクリル樹脂グラフトポリウレタン、ビニル樹脂グラフトポリエステル、ビニル樹脂グラフトポリウレタン、アクリレート樹脂グラフトポリエチレングリコール、等が挙げられる。バインダー成分の配合量は、塗布層に対する重量部で50重量部以下、さらには30重量部以下の範が好ましい。 In the coating layer, if necessary, a water-soluble or water-dispersible binder resin other than the polyvinyl alcohol may be used in combination. Binder resin is a polymer compound safety evaluation flow scheme (November 1985, sponsored by the Chemical Substances Council) with a high number average molecular weight (Mn) of 1000 or more by gel permeation chromatography (GPC) measurement. It can be defined as a molecular compound having film-forming properties. 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.

 さらに塗布層中には、必要に応じて架橋反応性化合物を含んでいてもよい。架橋反応性化合物としては、メチロール化あるいはアルキロール化した尿素系、メラミン系、グアナミン系、アクリルアミド系、ポリアミド系などの化合物、ポリアミン類、エポキシ化合物、オキサゾリン化合物、アジリジン化合物、ブロックイソシアネート化合物、シランカップリング剤、チタンカップリング剤、ジルコ-アルミネート系カップリング剤、金属キレート、有機酸無水物、有機過酸化物、熱または光反応性のビニル化合物や感光性樹脂などの多官能低分子化合物および高分子化合物から選択される。 Furthermore, the coating layer may contain a crosslinking reactive compound as required. Cross-linking reactive compounds include methylolated or alkylolized urea-based, melamine-based, guanamine-based, acrylamide-based, polyamide-based compounds, polyamines, epoxy compounds, oxazoline compounds, aziridine compounds, blocked isocyanate compounds, silane cups Polyfunctional low molecular 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.

 架橋反応性化合物は、塗布層に含まれる樹脂が有する官能基と架橋反応することで、塗布層の凝集性、表面硬度、耐擦傷性、耐溶剤性、耐水性を改良することができる。例えば、易接着樹脂の官能基が水酸基の場合、架橋反応性化合物としては、メラミン系化合物、ブロックイソシアネート化合物、有機酸無水物などが好ましく、易接着ポリエステルの官能基が有機酸およびその無水物の場合、架橋反応性化合物としてはエポキシ系化合物、メラミン系化合物、オキサゾリン系化合物、金属キレートなどが好ましく、易接着樹脂の官能基がアミン類の場合、架橋反応性化合物としてはエポキシ系化合物などが好ましく、易接着樹脂に含まれる官能基と架橋反応効率が高いものを選択して用いることが好ましい。メラミン化合物としては、アルキロールまたはアルコキシアルキロール化したメラミン系化合物であるメトキシメチル化メラミン、ブトキシメチル化メラミン等が例示され、メラミンの一部に尿素等を共縮合したものも使用できる。 The crosslinking reactive compound can improve the cohesiveness, surface hardness, scratch resistance, solvent resistance, and water resistance of the coating layer by crosslinking reaction with the functional group of the resin contained in the coating layer. 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. When the functional group of the easy-adhesion resin is an amine, an epoxy-based compound is 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 include methoxymethyl melamine and butoxymethylated melamine which are alkylol or alkoxyalkylol melamine compounds, and those obtained by co-condensing urea or the like with a part of melamine can also be used.

 架橋反応性化合物は反応性官能基が1分子中に2官能以上必ず含まれる限りにおいて、低分子量化合物であっても、反応性官能基を有する高分子重合体のいずれであってもよい。架橋反応性化合物の配合量は、塗布層に対する重量部で50重量部以下、さらには30重量部以下、特に15重量部以下の範囲が好ましい。 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 always contains two or more functional groups in one molecule. The blending 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 coating layer.

 バインダー樹脂と架橋剤とを任意割合で配合した場合、塗布層が密にバリア層を形成するためOLを一層効果的に抑制することができる。このため、ポリエステルフィルムからのOLを極力、粘着剤に付着させない、また、先の加工工程内で出さない効果がある。 When the binder resin and the cross-linking agent are blended in an arbitrary ratio, the coating layer forms a barrier layer densely, so that OL can be more effectively suppressed. 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.

 塗布層中は、必要に応じて塗布層の滑り性改良のために不活性粒子を含んでいてもよい。不活性粒子としては、無機不活性粒子、有機不活性粒子があり、無機不活性粒子としては、例えば、シリカゾル、アルミナゾル、炭酸カルシウム、酸化チタン等が挙げられる。有機不活性粒子としては、ポリスチレン系樹脂、ポリアクリル系樹脂、ポリビニル系樹脂による単独あるいは共重合体を含む微粒子、またはこれらと架橋成分を複合した架橋粒子に代表される有機粒子が挙げられる。これらの不活性粒子は軟化温度または分解温度が約200℃以上、さらには250℃以上、特に300℃以上であることが好ましい。不活性粒子の平均粒径(d)は、塗布層の平均膜厚を(L)とした際、1/3≦d/L≦3、さらには1/2≦d/L≦2の関係を満足するように選択するのが好ましい。 The coating layer may contain inert particles for improving the slipperiness of the coating layer as 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 has a relationship of 1/3 ≦ d / L ≦ 3, and further 1/2 ≦ d / L ≦ 2, when the average film thickness of the coating layer is (L). It is preferable to select so as to satisfy.

 塗布層は、必要に応じて界面活性剤、消泡剤、塗布性改良剤、増粘剤、低分子帯電防止剤、有機系潤滑剤、酸化防止剤、紫外線吸収剤、発泡剤、染料、顔料等の添加剤を少量含有していてもよい。これらの添加剤は単独で用いてもよいが、必要に応じて二種以上を併用してもよい。塗布層は、ポリエステルフィルムの片面だけに形成してもよいし、両面に形成してもよい。片面のみに形成する場合、その反対面には必要に応じて別種の塗布層を形成させ、さらに他の特性を付与することもできる。なお、塗布液のフィルムへの塗布性および接着性を改良するため、塗布前のフィルムに化学処理や放電処理等を施してもよい。 The coating layer is a surfactant, antifoaming agent, coating property improver, thickener, low molecular antistatic agent, organic lubricant, antioxidant, ultraviolet absorber, foaming agent, dye, pigment as necessary A small amount of such additives may be contained. These additives may be used alone or in combination of two or more as necessary. The coating layer 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.

 塗布層の形成に使用する塗布液は、通常、安全性や衛生性の観点から水を主たる媒体として調整されていることが好ましい。水を主たる媒体とする限りにおいて、水への分散を改良する目的あるいは造膜性能を改良する目的で少量の有機溶剤を含有していてもよい。有機溶剤は、主たる媒体である水と混合して使用する場合、水に溶解する範囲で使用することが好ましいが、長時間の放置で分離しないような安定した乳濁液(エマルジョン)であれば、水に溶解しない状態で使用してもよい。有機溶剤は単独で用いてもよいが、必要に応じて二種以上を併用してもよい。 The coating solution used for forming the coating layer is usually preferably adjusted with water as the main medium from the viewpoint of safety and hygiene. As long as water is the main medium, a small amount of an organic solvent may be contained for the purpose of improving the dispersion in water or improving the film forming performance. The organic solvent is preferably used as long as it is dissolved in water when mixed with water, which is the main medium. However, if it is a stable emulsion (emulsion) that does not separate after standing for a long time, Alternatively, it may be used in a state where it does not dissolve in water. The organic solvent may be used alone or in combination of two or more as necessary.

 ポリエステルフィルムの表面に塗布液を塗布する方法としては、原崎勇次著、槙書店、1979年発行、「コーティング方式」に示されるリバースロールコーター、グラビアコーター、ロッドコーター、エアドクターコーター等を使用することができる。 Use the reverse roll coater, gravure coater, rod coater, air doctor coater, etc. shown in “Coating Method” by Yuji Harasaki, Tsuji Shoten, published in 1979, as a method of applying the coating solution to the surface of the polyester film. Can do.

 塗布層を設ける方法は、特に制限されないが、ポリエステルフィルムを製造する工程中で塗布液を塗布する方法(インラインコーティング)が好適に採用される。具体的には、未延伸シート表面に塗布液を塗布して乾燥する方法、一軸延伸フィルム表面に塗布液を塗布して乾燥する方法、二軸延伸フィルム表面に塗布液を塗布して乾燥する方法等が挙げられる。これらの中では、未延伸フィルムまたは一軸延伸フィルム表面に塗布液を塗布後、フィルムに熱処理を行う過程で同時に塗布層を乾燥硬化する方法が経済的である。また、塗布層を形成する方法として、必要に応じ、前述の塗布方法の幾つかを併用した方法も採用し得る。具体的には、未延伸シート表面に第一層を塗布して乾燥し、その後、一軸方向に延伸後、第二層を塗布して乾燥する方法等が挙げられる。 The method of providing the coating layer is not particularly limited, but a method of applying a coating solution (in-line coating) in the process of manufacturing the polyester film is suitably employed. Specifically, a method of applying and drying a coating solution on the surface of an unstretched sheet, a method of applying and drying a coating solution on the surface of a uniaxially stretched film, and a method of applying and drying a coating solution on the surface of a biaxially stretched film Etc. Among these, it is economical to apply a coating solution on the surface of an unstretched film or a uniaxially stretched film, and then simultaneously dry and cure the coating layer in the process of heat-treating the film. Moreover, as a method for forming the coating layer, a method in which some of the above-described coating methods are used in combination can be adopted as necessary. Specifically, a method of applying a first layer on the surface of an unstretched sheet and drying, then stretching in a uniaxial direction, and then applying and drying a second layer can be used.

 インラインコーティングによって塗布層を設ける場合は、上述の一連の化合物を水溶液または水分散体として、固形分濃度が0.1~50重量%程度を目安に調整した塗布液をポリエステルフィルム上に塗布する要領にて積層ポリエステルフィルムを製造するのが好ましい。また、本発明の主旨を損なわない範囲において、水への分散性改良、造膜性改良等を目的として、塗布液中には少量の有機溶剤を含有していてもよい。有機溶剤は1種類のみでもよく、適宜、2種類以上を使用してもよい。 When providing a coating layer by in-line coating, apply the above-mentioned series of compounds as an aqueous solution or water dispersion on a polyester film with a coating solution adjusted to a solid content concentration of about 0.1 to 50% by weight. 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.

 ポリエステルフィルム上に塗布層を形成する際の乾燥および硬化条件に関しては、特に限定されるわけではなく、例えば、インラインコーティングにより塗布層を設ける場合、通常、70~280℃で3~200秒間を目安として熱処理を行うのが良い。また、必要に応じて熱処理と紫外線照射等の活性エネルギー線照射とを併用してもよい。さらにポリエステルフィルムには、予め、コロナ処理、プラズマ処理等の表面処理を施してもよい。 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 in-line coating, the standard is usually 70 to 280 ° C. for 3 to 200 seconds. It is better to perform heat treatment. Moreover, you may use together heat processing and active energy ray irradiation, such as ultraviolet irradiation, as needed. Furthermore, the polyester film may be subjected to surface treatment such as corona treatment or plasma treatment in advance.

 離型フィルムがポリビニルアルコールを含む塗布層を有する場合、離型フィルムを熱処理(180℃、10分間)した後、塗布層表面からジメチルホルムアミドにより抽出されるOL量は1.0mg/m以下であることが好ましい。OLが1.0mg/mを超える場合、工程汚染があり、粘着剤貼り合わせ時に、異物が発生し、製品の歩留まりが落ちるなどの不具合が生じることがある。 When the release film has a coating layer containing polyvinyl alcohol, the amount of OL extracted from the coating layer surface with dimethylformamide after heat treatment (180 ° C., 10 minutes) is 1.0 mg / m 2 or less. Preferably there is. When OL exceeds 1.0 mg / m 2 , there is a process contamination, and when the adhesive is bonded, a foreign matter may be generated, resulting in a problem such as a decrease in product yield.

 塗布層の膜厚は、通常0.002~1.0g/m、好ましくは0.005~0.5g/m、更に好ましくは0.01~0.2g/mの範囲である。膜厚が0.002g/m未満の場合は十分な密着性が得られない可能性があり、1.0g/mを超える場合は、外観や透明性、フィルムのブロッキング性が悪化する可能性がある。塗布層中の成分の分析は、例えば、TOF-SIMS等の表面分析によって行うことができる。 The thickness of the coating layer is usually in the range of 0.002 to 1.0 g / m 2 , preferably 0.005 to 0.5 g / m 2 , more preferably 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. Analysis of the components in the coating layer can be performed by surface analysis such as TOF-SIMS.

 なお、本発明においては、通常のOL含有量のポリエステルからなる層の少なくとも片側の表面に、OL含有量の少ないポリエステルを共押出積層した構造を有するフィルムであってもよく、かかる構造を有する場合、本発明の離型フィルムにおいて、析出したOLによる輝点を防止する効果が得られ、特に好ましい。 In the present invention, a film having a structure in which a polyester having a low OL content is coextruded and laminated on at least one surface of a layer composed of a polyester having a normal OL content may be used. In the release film of the present invention, the effect of preventing bright spots due to the precipitated OL is obtained, which is particularly preferable.

<離型層>
 本発明における離型層は、官能基としてアルケニル基を有するシリコーン樹脂(a)、官能基としてアルキル基を有するシリコーン樹脂(b)、粘着層への移行成分(c)、及び、白金系触媒(d)を含有するシリコーン系離型層である。
<Release layer>
The release layer in the present invention comprises a silicone resin (a) having an alkenyl group as a functional group, a silicone resin (b) having an alkyl group as a functional group, a migration component (c) to the adhesive layer, and a platinum catalyst ( It is a silicone release layer containing d).

 まず、アルケニル基を含む硬化型シリコーン樹脂は、ジオルガノポリシロキサンとして、分子鎖両末端トリメチルシロキシ基封鎖ジメチルシロキサン・メチルヘキセニルシロキサン共重合体(ジメチルシロキサン単位96モル%、メチルヘキセニルシロキサン単位4モル%)、分子鎖両末端ジメチルビニルシロキシ基封鎖ジメチルシロキサン・メチルヘキセニルシロキサン共重合体(ジメチルシロキサン単位97モル%、メチルヘキセニルシロキサン単位3モル%)、分子鎖両末端ジメチルヘキセニルシロキシ基封鎖ジメチルシロキサン・メチルヘキセニルシロキサン共重合体(ジメチルシロキサン単位95モル%、メチルヘキセニルシロキサン単位5モル%)が挙げられる。 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 / methyl-blocked dimethylhexenylsiloxy group blocked at both ends of the molecular chain Hexenylsiloxane copolymer (95 mol% of dimethylsiloxane units, 5 mol% of methylhexenylsiloxane units).

 次に、アルキル基を含む硬化型シリコーン樹脂は、オルガノハイドロジェンポリシロキサンとして、分子鎖両末端トリメチルシロキシ基封鎖メチルハイドロジェンポリシロキサン、分子鎖両末端トリメチルシロキシ基封鎖ジメチルシロキサン・メチルハイドロジェンシロキサン共重合体、分子鎖両末端ジメチルハイドロジェンシロキシ基封鎖メチルハイドロジェンポリシロキサン、分子鎖両末端ジメチルハイドロジェンシロキシ基封鎖ジメチルシロキサン・メチルハイドロジェンシロキサン共重合体が挙げられる。 Next, the curable silicone resin containing an alkyl group is a trimethylsiloxy group-blocked methylhydrogenpolysiloxane having both molecular chains and trimethylsiloxy group-blocked dimethylsiloxane / methylhydrogensiloxane as both organohydrogenpolysiloxanes. Examples thereof include a polymer, a dimethylhydrogensiloxy group-capped methylhydrogen polysiloxane having both molecular chains, and a dimethylsiloxane / methylhydrogensiloxane copolymer having both molecular chains having both ends dimethylhydrogensiloxy group-capped.

 本発明の離型フィルムは、離型層を基材レス両面粘着シートの粘着層に張り合わせて使用されるが、上記のシリコーン樹脂は、粘着層への移行成分を含有する。移行成分として典型的にはシリコーンオイルが使用される。シリコーンオイルは、ストレートシリコーンオイル、変性シリコーンオイルと称されるシリコーンオイルであり、以下のようなものが挙げられる。ストレートシリコーンとしては、ジメチルシリコーンオイル、メチルフェニルシリコーンオイル、メチルハイドロジェンシリコーンオイル等が挙げられる。また、変性シリコーンオイルとしては、側鎖型タイプのポリエーテル変性、アラルキル変性、フロロアルキル変性、長鎖アルキル変性、高級脂肪酸エステル変性、高級脂肪酸アミド変性、ポリエーテル・長鎖アルキル変性・アラルキル変性、フェニル変性、両末端型のポリエーテル変性、ポリエーテル・メトキシ変性などが挙げられる。ストレートシリコーンオイル、変性シリコーンオイル共に、非反応性の無官能オイルである。 The release film of the present invention is used by sticking the release layer to the adhesive layer of the base-less double-sided pressure-sensitive adhesive sheet, but the above-mentioned silicone resin contains a component that migrates to the adhesive layer. Silicone oil is typically used as the migration component. The silicone oil is a silicone oil called straight silicone oil or modified silicone oil, and examples thereof include the following. Examples of the straight silicone include dimethyl silicone oil, methylphenyl silicone oil, methyl hydrogen silicone oil, and the like. Further, as modified silicone oil, side chain type polyether modified, aralkyl modified, fluoroalkyl modified, long chain alkyl modified, higher fatty acid ester modified, higher fatty acid amide modified, polyether / long chain alkyl modified / aralkyl modified, Examples include phenyl modification, polyether modification at both ends, and polyether / methoxy modification. Both straight silicone oil and modified silicone oil are non-reactive, non-functional oils.

 移行成分の含有量は、5~20重量%、好ましくは10~13重量%、更に好ましくは0.1~5.0重量%である。移行成分の含有量が5%より低いと後述する速度依存性が高くなり、20重量%を超えると、硬化性が著しく低下し、密着性も悪化する不具合がある。 The content of the migration component is 5 to 20% by weight, preferably 10 to 13% by weight, more preferably 0.1 to 5.0% by weight. When the content of the transition component is lower than 5%, the speed dependency described later is increased, and when it exceeds 20% by weight, the curability is remarkably lowered and the adhesion is deteriorated.

 本発明で使用し得るシリコーン系樹脂塗剤の具体例としては、信越化学工業(株)製のKS-774、KS-775、KS-778、KS-779H、KS-847H、KS-856、X-62-2422、X-62-2461;ダウ・コーニング・アジア(株)製のDKQ3-202、DKQ3-203、DKQ3-204、DKQ3-205、DKQ3-210;東芝シリコーン(株)製のYSR-3022、TPR-6700、TPR-6720、TPR-6721;東レ・ダウ・コーニング(株)製のLTC300B、LTC303E、LTC310、LTC314、SRX357、BY24-749、SD7333、BY24-179、SP7015、SP7259、SD7220、SD7226、SD7229等が挙げられる。さらに離型層の剥離性等を調整するために剥離コントロール剤を併用してもよい。 Specific examples of silicone-based resin coatings that can be used in the present invention include KS-774, KS-775, KS-778, KS-779H, KS-847H, KS-856, X, manufactured by Shin-Etsu Chemical Co., Ltd. -62-2422, X-62-2461; DKQ3-202, DKQ3-203, DKQ3-204, DKQ3-205, DKQ3-210 manufactured by Dow Corning Asia Ltd .; YSR- manufactured by Toshiba Silicone Corp. 3022, TPR-6700, TPR-6720, TPR-6721; LTC300B, LTC303E, LTC310, LTC314, SRX357, BY24-749, SD7333, BY24-179, SP7015, SP7259, SD7220, manufactured by Toray Dow Corning Co., Ltd. SD7226, SD7229, etc.Further, a release control agent may be used in combination to adjust the release property of the release layer.

 上記のシリコーン系樹脂塗剤は、官能基としてアルケニル基を有するシリコーン樹脂(a)、官能基としてアルキル基を有するシリコーン樹脂(b)、粘着層への移行成分(c)から成るが、官能基としてアルケニル基を有するシリコーン樹脂(a)、官能基としてアルキル基を有するシリコーン樹脂(b)の比率は、(b)/(a)は、通常0.5~2重量比である。なお、本発明においては官能基としてアルケニル基およびアルキル基を有するシリコーン樹脂を使用してもよい。 The silicone-based resin coating material is composed of a silicone resin (a) having an alkenyl group as a functional group, a silicone resin (b) having an alkyl group as a functional group, and a component (c) for transferring to an adhesive layer. The ratio of the silicone resin having an alkenyl group as (a) and the silicone resin having an alkyl group as a functional group (b) is (b) / (a) is usually 0.5 to 2 weight ratio. In the present invention, a silicone resin having an alkenyl group and an alkyl group as a functional group may be used.

 ポリエステルフィルムに離型層を設ける方法としては、前述の塗布層の場合と同様に、従来公知の塗工方式を用いることができる。離型層を形成する際の塗布量は、通常0.01~1g/mの範囲である。 As a method for providing the release layer on the polyester film, a conventionally known coating method can be used as in the case of the above-mentioned coating layer. The coating amount when forming the release layer is usually in the range of 0.01 to 1 g / m 2 .

 離型層が設けられていない面には、接着層、帯電防止層、オリゴマー析出防止層等の塗布層を設けてもよく、また、ポリエステルフィルムにはコロナ処理、プラズマ処理等の表面処理を施してもよい。 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 is subjected to a surface treatment such as corona treatment or plasma treatment. May be.

 本発明においては、離型層をきれいかつ頑丈にするため、付加型の反応を促進する白金系触媒を用いる。本成分としては、塩化白金酸、塩化白金酸のアルコール溶液、塩化白金酸とオレフィンとの錯体、塩化白金酸とアルケニルシロキサンとの錯体等の白金系化合物、白金黒、白金担持シリカ、白金担持活性炭が例示される。離型層中の白金系触媒含有量は、通常0.3~3.0重量%、好ましくは0.5~2.0重量%の範囲が良い。離型層中の白金系触媒含有量が0.3重量%よりも低い場合、剥離力の不具合や、塗布層での硬化反応が不十分になるため、面状悪化などの不具合を生じる場合があり、一方、離型層中の白金系触媒含有量が3.0重量%を超える場合には、コストがかかる、また、反応性が高まり、ゲル異物が発生する等の工程不具合を生じてしまうことがある。 In the present invention, a platinum-based catalyst that promotes an addition-type reaction is used in order to make the release layer clean and robust. 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 release layer is usually 0.3 to 3.0% by weight, preferably 0.5 to 2.0% by weight. When the platinum-based catalyst content in the release layer is lower than 0.3% by weight, there may be 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, when the platinum-based catalyst content in the release layer exceeds 3.0% by weight, the cost is increased, and the process becomes defective due to increased reactivity and generation of gel foreign matter. Sometimes.

 また、付加型の反応は非常に反応性が高いため、場合によっては、反応抑制剤として、アセチレンアルコールを添加することがある。その成分は、炭素-炭素3重結合と水酸基を有する有機化合物であるが、好ましくは、3-メチル-1-ブチン-3-オール、3,5-ジメチル-1-ヘキシン-3-オールおよびフェニルブチノールからなる群から選択される化合物である。 Further, since the addition type reaction is very reactive, acetylene alcohol may be added as a reaction inhibitor in some cases. The component is an organic compound having a carbon-carbon triple bond and a hydroxyl group, preferably 3-methyl-1-butyn-3-ol, 3,5-dimethyl-1-hexyn-3-ol and phenyl. It is a compound selected from the group consisting of butinol.

<剥離力>
 本発明における、剥離力とは、両面粘着テープ(日東電工製「No.31B」)を離型層面に貼り付け、室温にて1時間放置した後に、基材フィルムと剥離角度180°、任意の引張速度でテープを剥離したときに引張試験機で測定した値を言う。
<Peeling force>
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.

 本発明において剥離力を調整する方法は、離型層中の組成を選択することにより達成することができるが、その他の手段も採用でき、主にシリコーン離型層の離型剤の種類を、所望の剥離力に応じて変更することが好ましく、さらには、剥離力は用いる離型剤の塗布量に大きく依存するため、その離型剤の塗布量を調整する方法が更に好ましい。 The method for adjusting the 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, It is preferable to change according to the desired peeling force. 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.

 本発明においては、日東電工株式会社製No.31Bテープによる残留接着率は、通常65%~90%、好ましくは、70%~85%である。残留接着率が65%より低いと、移行性が高く、粘着剤加工時にロール汚れや粘着剤面に移行して、粘着剥離力低下などが生じてしまう。また、残留接着率が90%以上となると、速度依存性を小さく抑えることができない。 In the present invention, Nitto Denko Corporation No. The residual adhesion rate with 31B tape is usually 65% to 90%, preferably 70% to 85%. When the residual adhesion rate is lower than 65%, the transferability is high, and the adhesive moves to roll dirt or the adhesive surface during the adhesive processing, resulting in a decrease in adhesive peeling force. Further, when the residual adhesion rate is 90% or more, the speed dependency cannot be reduced.

 本発明の離型フィルムの剥離力の値は、300mm/分速度域での低速剥離力が10~20mN/cmの範囲である。当該剥離力が10mN/cm未満の場合、剥離力が軽くなりすぎて本来剥離する必要がない場面においても容易に剥離する不具合を生じる。剥離力が20mN/cmを超える場合、剥離力の重い方の離型フィルムとの剥離力差が小さくなり、剥離工程で不具合を生じたり、剥離力の重い方の離型フィルムの選定幅が狭くなったりする等の問題がある。 The value of the peel force of the release film of the present invention is such that the low speed peel force in the range of 300 mm / min is 10 to 20 mN / cm. 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 off. If the peel force exceeds 20 mN / cm, the difference in peel force between the release film with the greater peel force will be small, causing problems in the peel process, and the selection range for the release film with the greater peel force will be narrow. There are problems such as becoming.

 さらに、加工性を考慮に入れた10000mm/分速度域での高速剥離力は、上記低速剥離力の2.5倍以下である。当該剥離力の比が2.5倍よりも大きい場合、剥離力が重い方の離型フィルムとの剥離力差が小さくなり、剥離工程で剥離が上手くできなかったり、粘着剤ごと剥がれてしまったりする。 Furthermore, the high speed peeling force in the 10,000 mm / min speed region taking into consideration workability is 2.5 times or less of the above low speed peeling force. If the peel force ratio is larger 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 may be peeled off. To do.

 本発明の離型フィルムの離型層のマルテンス硬度は、通常400N/mm以上、好ましくは、450N/mm以上である。離型層のマルテンス硬度が400N/mmよりも小さい場合、離型フィルムの剥離力において、剥離速度依存性が大きくなる、また、フィルム表面が傷つきやすく、OLが発生し易くなる、等の不具合が生じることがある。 Martens hardness of the release layer of the release film of the present invention is usually 400 N / mm 2 or more, preferably, 450 N / mm 2 or more. When the Martens hardness of the release layer is less than 400 N / mm 2 , the release film dependency of the release film increases, and the film surface is easily damaged and OL is likely to occur. May occur.

 上記のマルテンス硬度とは、三角錐型の圧子を使用した硬度測定機を用いて、表層の計装化押し込み硬さ試験によって求められる硬度を意味し、115°三角錐圧子、0.10mNの試験力で測定した値である。 The above-mentioned Martens hardness means a hardness obtained by an instrumented indentation hardness test on a surface layer using a hardness measuring machine using a triangular pyramid indenter, and a test of 115 ° triangular pyramid indenter and 0.10 mN. It is a value measured by force.

 本発明の離型フィルムについては、用途に応じて、工程の光学検査等で異物や光干渉色の発生を行う場合がある。工程の光学検査等で異物や光干渉色の発生を低減するには、離型フィルムをマイクロ波方式分子配向計で測定したMOR_C値の最適化が非常に重要である。ポリエステルフィルムのMOR_C値の範囲を満足させるための手段は、製膜時ににおいて、所望のフィルム厚みに対して、延伸条件を適宜選択することにある。 For the release film of the present invention, foreign matter or light interference color may be generated in the optical inspection of the process depending on the application. In order to reduce the generation of foreign matter and light interference colors in optical inspection of the process, etc., it is very important to optimize the MOR_C value obtained by measuring the release film with a microwave molecular orientation meter. A means for satisfying the range of the MOR_C value of the polyester film is to appropriately select the stretching conditions for the desired film thickness during film formation.

 ポリエステルフィルムのMOR_C値は、通常1.5~3.0、好ましくは1.8~2.7、更に好ましくは2.1~2.4である。MOR_C値が3.0よりも大きい場合には、離型層の均一性に欠けたり、光学検査がある場合において、光干渉色が見えやすくなる等の不具合が生じたりする。MOR_C値が1.5よりも小さい場合には、離型フィルム自体の生産歩留まり悪くなってしまう等の問題がある。 The MOR_C value of the polyester film is usually 1.5 to 3.0, preferably 1.8 to 2.7, more preferably 2.1 to 2.4. When the MOR_C value is larger than 3.0, the release layer is not uniform, and in the case where there is an optical inspection, problems such as easy appearance of the light interference color may occur. When the MOR_C value is smaller than 1.5, there is a problem that the production yield of the release film itself is deteriorated.

 以下、本発明を実施例によりさらに詳細に説明するが、本発明はその要旨を越えない限り、以下の実施例に限定されるものではない。また、本発明で用いた測定法および評価方法は次のとおりである。 Hereinafter, the present invention will be described in more detail with reference to examples. However, the present invention is not limited to the following examples unless it exceeds the gist. The measurement method and evaluation method used in the present invention are as follows.

(1)ポリエステルの固有粘度の測定:
 ポリエステルに非相溶な他のポリマー成分および顔料を除去したポリエステル1gを精秤し、フェノール/テトラクロロエタン=50/50(重量比)の混合溶媒100mlを加えて溶解させ、30℃で測定した。
(1) Measurement of intrinsic viscosity of polyester:
1 g of polyester from which other polymer components and pigments incompatible with polyester were removed was precisely weighed, 100 ml of a mixed solvent of phenol / tetrachloroethane = 50/50 (weight ratio) was added and dissolved, and measurement was performed at 30 ° C.

(2)平均粒径(d50:μm)の測定:
 遠心沈降式粒度分布測定装置(株式会社島津製作所社製SA-CP3型)を使用して測定した等価球形分布における積算(重量基準)50%の値を平均粒径とした。
(2) Measurement of average particle diameter (d50: μm):
The value of 50% of integration (weight basis) in the equivalent spherical distribution measured using a centrifugal sedimentation type particle size distribution measuring apparatus (SA-CP3 type manufactured by Shimadzu Corporation) was defined as the average particle diameter.

(3)ポリエステルフィルムの透過率測定:
 JIS-K7105に準じ、日本電色工業社製積分球式濁度計NDH-300Aによりポリエステルフィルムの全光線透過率を測定した。
(3) Transmittance measurement of polyester film:
The total light transmittance of the polyester film was measured with an integrating sphere turbidimeter NDH-300A manufactured by Nippon Denshoku Industries Co., Ltd. according to JIS-K7105.

(4)ポリエステルフィルムの加熱収縮率測定:
 ポリエステルフィルムを縦長さの方向(以後、MDと略する)と横幅の方向(以後、TDと略する)にそれぞれ、任意の長さL(cm)でサンプリングする。続いて、そのサンプルをオーブンで160℃、5分の加熱を行い、そのサンプルをオーブンから取り出して長さl(cm)を測定する。この操作を3回行い、平均値を加熱収縮率の値として採用する。下記式で加熱収縮率は算出できる。
 加熱収縮率(%)={(L-l)/L}×100
(4) Heat shrinkage measurement of polyester film:
The polyester film is sampled at an arbitrary length L (cm) in the longitudinal direction (hereinafter abbreviated as MD) and the lateral width direction (hereinafter abbreviated as TD). 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 rate (%) = {(L−l) / L} × 100

(5)塗布層中触媒量測定:
 SAICASを用いて、試料フィルムに斜め切削を行い、断面を露出させた。その後、TOF-SIMS(飛行時間型質量分析マススペクトル)を用いて、ポリエステルフィルム塗布層中に含まれる白金を含む触媒量を求めた。
(5) Measurement of amount of catalyst in coating layer:
Using SAICAS, the sample film was obliquely cut to expose the cross section. Thereafter, 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).

(6)移行成分量測定:
 トルエンで固形分濃度4重量%に希釈したシリコーン樹脂15gに対して白金触媒0.02重量%0.004gを添加し、攪拌後、テフロン(登録商標)製のシートで作成した箱に入れ、150℃1時間熱硬化する(サンプル1)。移行成分を添加する場合(後述の比較例2に該当する)は、シリコーン樹脂の固形分に対して30重量%添加する。サンプル1を1日トルエンに浸漬し、取り出したサンプルを、120℃30分乾燥し、室温になるまで、放冷する(サンプル2)。下記式より以降成分量を算出した。
 移行成分量(重量%)=(サンプル1の重量-サンプル2の重量)÷サンプル1の重量×100
(6) Measurement of migration component amount:
Add 0.04 wt% 0.004 g of platinum catalyst to 15 g of silicone resin diluted with toluene to a solid content concentration of 4 wt%, and after stirring, put it in a box made of a sheet made of Teflon (registered trademark). Heat cure at 1 ° C. for 1 hour (Sample 1). When adding a migration component (corresponding to Comparative Example 2 described later), 30% by weight is added to the solid content of the silicone resin. Sample 1 is immersed in toluene for 1 day, and the sample taken out is dried at 120 ° C. for 30 minutes and allowed to cool to room temperature (sample 2). The component amount was calculated from the following formula.
Migration component amount (% by weight) = (weight of sample 1−weight of sample 2) ÷ weight of sample 1 × 100

(7)離型フィルムの移行性評価接着率:
 試料フィルムをA4大に切り取り、離型面に75μm厚の2軸延伸PETフィルム(三菱化学ポリエステルフィルム株式会社製:ダイアホイルT100-75)を重ねて温度60℃、圧力1MPaの条件で2時間プレスする。この離型面に押し当てた75μm厚フィルムを移行性評価フィルムとする。未処理のPETフィルムにも同様にして75μm厚2軸延伸PETフィルム(同)を押し当て、基準フィルムとする。それぞれのフィルムの押し当てた面に粘着テープ(日東電工(株)製「No.31B」)を貼り付けた後、50mm×300mmのサイズにカットし、室温にて1時間放置後の剥離力を測定した。剥離力は(株)島津製作所製「Ezgraph」を使用し、引張速度0.3(m/min)の条件下、180°剥離を行った。
 移行性評価接着率(%)=(移行性評価フィルムの剥離力÷基準フィルムの剥離力)×100
 移行性の大きなフィルムでは押し当てたフィルムに多くのシリコーンが付着するため、粘着テープの剥離力が小さくなり、移行性評価接着率(%)も低下する。
(7) Transferability evaluation adhesion rate of release film:
The sample film was cut to A4 size, and 75μm thick biaxially stretched PET film (Mitsubishi Chemical Polyester Film Co., Ltd .: Diafoil T100-75) was layered on the release surface and pressed for 2 hours under the conditions of temperature 60 ° C and pressure 1MPa. To do. A 75 μm-thick film pressed against this release surface is used as a migration evaluation film. Similarly, a 75 μm-thick biaxially stretched PET film (same as above) is pressed against an untreated PET film as a reference film. Adhesive tape (“No. 31B” manufactured by Nitto Denko Corporation) is applied to the pressed surface of each film, then cut to a size of 50 mm × 300 mm, and the peel strength after standing for 1 hour at room temperature. It was measured. The peeling force was “Ezgraph” manufactured by Shimadzu Corporation, and 180 ° peeling was performed under the condition of a tensile speed of 0.3 (m / min).
Transferability evaluation adhesion rate (%) = (Peeling force of transferability evaluation film ÷ Peeling force of reference film) × 100
In a film having a high migration property, since a lot of silicone adheres to the pressed film, the peeling force of the adhesive tape is reduced, and the migration evaluation adhesion rate (%) is also lowered.

(8)離型フィルムの剥離力(F)の評価:
 試料フィルムの離型層表面に両面粘着テープ(日東電工製「No.31B」)の片面を貼り付けた後、50mm×300mmのサイズにカットした後、室温にて1時間放置後の剥離力を測定する。剥離力は、引張試験機((株)インテスコ製「インテスコモデル2001型」)を使用し、引張速度300mm/分、さらに、10000mm/分の条件下、180°剥離を行った。次のような基準で判断する。
(8) Evaluation of release force (F) of release film:
After attaching one side of a double-sided adhesive tape (“No. 31B” manufactured by Nitto Denko) to the surface of the release layer of the sample film, the sample film was cut to a size of 50 mm × 300 mm and then peeled after being left at room temperature for 1 hour. taking measurement. For the peeling force, a tensile tester (“Intesco model 2001 type” manufactured by Intesco Co., Ltd.) was used, and 180 ° peeling was performed under the conditions of a tensile speed of 300 mm / min and further 10,000 mm / min. Judgment is based on the following criteria.

<300mm/分での剥離力>
 ○:10~20mN/cmの範囲である。
 ×:10mN/cmより小さい、もしくは、20mN/cmより大きい。
<Peeling force at 300 mm / min>
○: A range of 10 to 20 mN / cm.
X: Less than 10 mN / cm or more than 20 mN / cm.

<10000mm/分での剥離力と300mm/分での剥離力の比較>
 下式にて求めた値で判断した。
(10000mm/分剥離力(mN/cm))÷(300mm/分剥離力(mN/cm))
 ○:2.5以下である。
 ×:2.5より大きい。
<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.
X: Greater than 2.5.

(9)離型特性:
 粘着層を有する積層フィルムより離型フィルムを剥がした時の状況より、離型特性を評価した。
 ○:離型フィルムがきれいに剥がれ、粘着剤が離型層に付着する現象が見られない。
 △:離型フィルムは剥がれるが、速い速度で剥離した場合に粘着剤が離型層に付着する。
 ×:離型フィルムに粘着剤が付着する、上手く剥がれない。
(9) Mold 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.
(Triangle | delta): Although a release film peels, an adhesive adheres to a release layer when it peels at a quick speed.
X: Adhesive adheres to the release film and does not peel off well.

(10)ポリエステルフィルムのコート表面の硬度測定:
 ポリエステルフィルムの表層に対して、島津製作所社製のダイナミック超微小高度計(DUH-211)を用いて、三角錐圧子(稜間角115°、ベルコビッチタイプ)、試験力:0.10mN、負荷保持速度:0.0060mN/sec.、負荷保持時間:2sec.の条件で測定を行ない、上記試験力に対する押込み深さからマルテンス硬さを算出した。なお、測定回数は12回で、それらの平均値を採った。
(10) Measurement of hardness of polyester film coat surface:
Using a dynamic ultra-micro altimeter (DUH-211) manufactured by Shimadzu Corporation on the surface layer of the polyester film, a triangular pyramid indenter (angle between ridges 115 °, Belkovic type), test force: 0.10 mN, load Holding speed: 0.0060 mN / sec. Load holding time: 2 sec. The Martens hardness was calculated from the indentation depth with respect to the test force. The number of measurements was 12, and the average value was taken.

(11)アンカー層表面から抽出されるOLの測定:
 あらかじめ、未熱処理の離型フィルムを空気中、180℃で10分間加熱する。その後、熱処理をした該フィルムを上部が開いている縦横10cm、高さ3cmの箱の内面にできるだけ密着させて箱形の形状とする。塗布層を設けている場合は塗布層面が内側となるようにする。次いで、上記の方法で作成した箱の中にDMF(ジメチルホルムアミド)4mlを入れて3分間放置した後、DMFを回収する。回収したDMFを液体クロマトグラフィー(島津製作所製:LC-7A)に供給して、DMF中のOL量を求め、この値を、DMFを接触させたフィルム面積で割って、フィルム表面OL量(mg/m)とする。
(11) Measurement of OL extracted from the anchor layer surface:
In advance, an unheat-treated release film is heated in air at 180 ° C. for 10 minutes. 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 a liquid chromatography (manufactured by Shimadzu Corporation: LC-7A) to determine the amount of OL in DMF, and this value was divided by the film area in contact with DMF to obtain the amount of OL on the film surface (mg / M 2 ).

 DMF中のオリゴマー量は、標準試料ピーク面積と測定試料ピーク面積のピーク面積比より求めた(絶対検量線法)。標準試料の作成は、あらかじめ分取したOL(環状三量体)を正確に秤量し、正確に秤量したDMFに溶解し作成した。標準試料の濃度は、0.001~0.01mg/mlの範囲が好ましい。なお、液体クロマトグラフの条件は下記のとおりとした。 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.

 移動相A:アセトニトリル
 移動相B:2%酢酸水溶液
 カラム:三菱化学(株)製『MCI GEL ODS 1HU』
 カラム温度:40℃
 流速:1ml/分
 検出波長:254nm 
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

(12)ポリエステルフィルムのマイクロ波分子配向計によるMOR_C値測定:
 王子計測機器株式会社製のマイクロ波方式分子配向計を用い、透過マイクロ波強度パターンからMOR_C値を求めた。
(12) MOR_C value measurement of polyester film by microwave molecular orientation meter:
The MOR_C value was determined from the transmission microwave intensity pattern using a microwave molecular orientation meter manufactured by Oji Scientific Instruments.

(13)ポリエステルフィルムのマイクロ波分子配向計によるMOR_C値測定:
 王子計測機器株式会社製のマイクロ波方式分子配向計を用い、透過マイクロ波強度パターンからMOR_C値を求めた。次のような基準で判断する。
 ○:2.0~2.5の範囲である。
 △:1.5~1.9、もしくは、2.6~3.0の範囲である。
 ×:1.5%よりも低い、もしくは、3.0よりも高い。
(13) MOR_C value measurement of polyester film by microwave molecular orientation meter:
The MOR_C value was determined from the transmission microwave intensity pattern using a microwave molecular orientation meter manufactured by Oji Scientific Instruments. Judgment is based on the following criteria.
○: The range is from 2.0 to 2.5.
Δ: The range is 1.5 to 1.9 or 2.6 to 3.0.
X: It is lower than 1.5% or higher than 3.0.

(14)実用特性:
<反射光下での目視検査性>
 偏光板検査を考慮に入れて、フィルム上に離型剤を塗布しドライヤー温度120℃、ライン速度30m/minの条件で得た離型フィルムの幅方向が、偏光フィルムの配向軸と平行となるように、粘着剤を介して離型フィルムを偏光フィルムに密着させ偏光板とし、蛍光灯反射下で偏光板を目視にて観察し、反射光下での目視検査性を下記基準に従い評価した。なお、測定の際には、A4サイズのサンプルを切り出して実施した。
「判定基準」
 ○:検査性良好である。
 △:ほぼ問題なく検査できる。
 ×:検査性不良である。
 ○および△のものが実使用上問題のないレベルである。
(14) Practical properties:
<Visual inspection under reflected light>
Taking the polarizing plate inspection into consideration, the width direction of the release film obtained by applying a release agent on the film and having a dryer temperature of 120 ° C. and a line speed of 30 m / min is parallel to the alignment axis of the polarizing film. As described above, the release film was closely adhered to the polarizing film through an adhesive to form a polarizing plate. The polarizing plate was visually observed under reflection of a fluorescent lamp, and the visual inspection property under reflected light was evaluated according to the following criteria. In the measurement, an A4 size sample was cut out.
"Criteria"
○: Good inspectability.
Δ: Inspection can be performed almost without any problem.
X: Inspectability is poor.
○ and △ are the levels where there is no problem in actual use.

<クロスニコル下での目視検査性>
 偏光板検査を考慮に入れて、フィルム上に離型剤を塗布しドライヤー温度120℃、ライン速度30m/minの条件で得た離型フィルムの幅方向が、偏光フィルムの配向軸と平行となるように、粘着剤を介して離型フィルムを偏光フィルムに密着させ偏光板とした。ここで上記偏光板を作成する際、粘着剤と偏光フィルムとの間に50μm以上の大きさを持つ黒色の金属粉(異物)を50個/mとなるように混入させた。このようにして得られた異物を混入させた偏光板離型フィルム上に配向軸が離型フィルム幅方向と直交するように検査用の偏光板を重ね合わせ、偏光板側より白色光を照射し、検査用の偏光板より目視にて観察し、クロスニコル下で粘着剤と偏光フィルムとの間に混入させた異物を見いだせるかどうかを下記基準に従い評価した。なお、測定の際には、得られたフィルムの幅方向に対し中央部と両端部の計3ヶ所から、それぞれA4サイズのサンプルを切り出して実施した。
「判定基準」
 ○:異物認知性良好である。
 △:比較的問題なく異物認知できる。
 ×:異物認知性不良である。
 ○および△のものが実使用上問題のないレベルである。
 上記判定基準中、○以上のものが実使用上問題なく使用できるレベルである。
<Visual inspection under crossed Nicols>
Taking the polarizing plate inspection into consideration, the width direction of the release film obtained by applying a release agent on the film and having a dryer temperature of 120 ° C. and a line speed of 30 m / min is parallel to the alignment axis of the polarizing film. As described above, the release film was adhered to the polarizing film through the pressure-sensitive adhesive to obtain a polarizing plate. Here, when the polarizing plate was prepared, black metal powder (foreign matter) having a size of 50 μm or more was mixed between the pressure-sensitive adhesive and the polarizing film so as to be 50 / m 2 . A polarizing plate for inspection is superimposed on the polarizing plate release film mixed with the foreign matter thus obtained so that the orientation axis is orthogonal to the width direction of the release film, and white light is irradiated from the polarizing plate side. Then, it was visually observed from a polarizing plate for inspection, and whether or not a foreign matter mixed between the adhesive and the polarizing film was found under crossed Nicols was evaluated according to the following criteria. In the measurement, A4 size samples were cut out from a total of three locations in the center and both ends in the width direction of the obtained film.
"Criteria"
○: Good foreign body recognition.
Δ: Foreign matter can be recognized with relatively no problem.
X: Foreign matter recognition is poor.
○ and △ are the levels where there is no problem in actual use.
Among the above criteria, those above ○ are levels that can be used without any problem in actual use.

(15)総合評価:
 製膜性、生産性、検査特性等、全てを考慮に入れた評価を行う。次のような基準で判断する。
 ○:生産しても充分に製品として供給できる。
 △:生産性が良い、かつ、光学検査での不具合の頻度が少ない。
 ×:生産性が悪い。光学検査での不具合が多発する。
(15) Overall evaluation:
An evaluation is performed in consideration of film forming properties, productivity, inspection characteristics, etc. Judgment is based on the following criteria.
○: Even if it is produced, it can be supplied as a product.
Δ: Productivity is good and the frequency of defects in optical inspection is low.
X: Productivity is poor. There are many problems with optical inspection.

 実施例および比較例において使用したポリエステルは、以下のようにして準備したものである。
<ポリエステル(a)の製造方法>
 テレフタル酸ジメチル100重量部とエチレングリコール60重量部とを出発原料とし、触媒としてテトラブトキシチタネートを加えて反応器にとり、反応開始温度を150℃とし、メタノールの留去とともに徐々に反応温度を上昇させ、3時間後に230℃とした。4時間後、実質的にエステル交換反応を終了させた後、4時間重縮合反応を行った。
 すなわち、温度を230℃から徐々に昇温し280℃とした。一方、圧力は常圧より徐々に減じ、最終的には0.3mmHgとした。反応開始後、反応槽の攪拌動力の変化により、極限粘度0.61に相当する時点で反応を停止し、窒素加圧下ポリマーを吐出させ、極限粘度0.61のポリエステル(a)を得た。
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.

<ポリエステル(b)の製造方法>
 ポリエステル(a)の製造方法において、エチルアシッドフォスフェートを添加後、平均粒子径0.8μmの合成炭酸カルシウム粒子のエチレングリコールスラリーを粒子のポリエステルに対する含有量が1重量%となるように添加した以外は、ポリエステル(a)の製造方法と同様の方法を用いてポリエステル(b)を得た。得られたポリエステル(b)は極限粘度0.60であった。
<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.

<ポリエステル(c)の製造>
 テレフタル酸ジメチル100重量部とエチレングリコール60重量部とを出発原料とし、触媒として酢酸マグネシウム四水塩を加えて反応器にとり、反応開始温度を150℃とし、メタノールの留去とともに徐々に反応温度を上昇させ、3時間後に230℃とした。
 4時間後、実質的にエステル交換反応を終了させた。この反応混合物にエチルアシッドフォスフェートを添加した後、重縮合槽に移し、三酸化アンチモン0.04部を加えて、4時間重縮合反応を行った。すなわち、温度を230℃から徐々に昇温し280℃とした。
 一方、圧力は常圧より徐々に減じ、最終的には0.3mmHgとした。反応開始後、反応槽の攪拌動力の変化により、固有粘度0.45に相当する時点で反応を停止し、窒素加圧下ポリマーを吐出させ、ポリエステルのチップ(c)を得た。このポリエステルの固有粘度は0.45であった。
<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.

<ポリエステル(d)の製造>
 このポリエステルチップを固相重縮合法にて固有粘度を上げた。予備結晶化槽にて170℃の窒素雰囲気化にて0.5時間処理した後、不活性ガスを流す塔式乾燥機を用い、200℃の温度下にて水分率が0.005%になるまで乾燥した。その後固相重合槽へ送り、240℃にて3時間、固相重合を行い固有粘度0.70のポリエステル(d)を得た。
<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.

<ポリエステル(e)の製造>
 ポリエステル(d)を製造する際、固相重合槽にて5時間固相重合を行い、固有粘度0.80のポリエステル(e)を得た。
<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.

 実施例1:
(ポリエステルフィルムの製造)
 表層の原料としてポリエステル(e)70重量%と、ポリエステル(b)30重量%を混合し、中間層の原料として、ポリエステル(a)84重量%とポリエステル(b)16重量%を混合し、2台のベント付き押出機に各々供給し、290℃で溶融押出した後、静電印加密着法を用いて表面温度を40℃に設定した冷却ロール上で冷却固化して未延伸シートを得た。次いで、100℃にて縦方向に2.8倍延伸した後、テンター内で予熱工程を経て120℃で5.1倍の横延伸を施した後、220℃で10秒間の熱処理を行い、その後180℃で幅方向に4%の弛緩を加え、幅4000mmのマスターロールを得た。このマスターロールの端から1400mmの位置よりスリットを行い、コアに1000m巻き取りし、ポリエステルフィルムを得た。得られたフィルムの全厚みは50μm(層構成:表層2.5μm/中間層45μm/表層2.5μm)であった。
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., then subjected to a preheating step in a tenter and subjected to a transverse stretching of 5.1 times at 120 ° C., followed by heat treatment at 220 ° C. for 10 seconds, 4% relaxation was added in the width direction at 180 ° C. 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 50 μm (layer structure: surface layer 2.5 μm / intermediate layer 45 μm / surface layer 2.5 μm).

 得られたポリエステルフィルムに、下記に示す離型剤組成-Aからなる離型剤を塗布量(乾燥後)が0.12g/mになるようにリバースグラビアコート方式により塗布し、ドライヤー温度120℃、ライン速度30m/分の条件でロール状の離型ポリエステルフィルムを得た。得られた離型ポリエステルフィルムは、300mm/分速度域での剥離力が14mN/cm離型フィルムで、かつ、10000mm/分速度域での剥離力が32mN/cmであった。 A release agent composed of release agent composition-A shown below was applied to the obtained polyester film by a reverse gravure coating method so that the coating amount (after drying) was 0.12 g / m 2 , and a dryer temperature of 120 A roll-shaped release polyester film was obtained under the conditions of ° C and a line speed of 30 m / min. The obtained release polyester film had a release force of 14 mN / cm at a speed of 300 mm / min and a release force of 32 mN / cm at a speed of 10,000 mm / min.

<離型剤組成-A>
 硬化型シリコーン樹脂(LTC303E:東レ・ダウコーニング製)
                               20部
 付加型白金触媒(SRX212:東レ・ダウコーニング製)  0.2部
 MEK/トルエン/n-ヘプタン混合溶媒(混合比率は1:1:1)
 離型剤組成-Aの移行性分量:15重量%
<Releasing agent composition-A>
Curable silicone resin (LTC303E: manufactured by Toray Dow Corning)
20 parts addition type platinum catalyst (SRX212: manufactured by Toray Dow Corning) 0.2 part MEK / toluene / n-heptane mixed solvent (mixing ratio is 1: 1: 1)
Release agent composition-A transferable amount: 15% by weight

 得られたポリエステルフィルムは、下記方法で偏向板を作成し、光学特性の検査性と剥離特性の評価を行った。得られた離型フィルムは反射による検査性良好、異物認知性良好であり、かつ、偏光板綺麗に剥がれ、粘着剤が離型層に付着する現象が見られなかった。 For the obtained polyester film, a deflector plate was prepared by the following method, and optical property inspection and peeling properties were evaluated. The obtained release film had good inspection by reflection and good recognition of foreign matter, and the polarizing plate was peeled off cleanly, and the phenomenon that the adhesive adhered to the release layer was not observed.

<離型フィルム付き偏光板の製造>
 偏光板に下記に示すアクリル粘着剤を、乾燥後の厚みが25μmとなるように塗布し、130℃の乾燥炉内を30秒で通過させた後、離型フィルムを貼り合わせ、粘着剤を介して離型フィルムと偏光フィルムが密着された離型フィルム付き偏光板を作成した。フィルムの貼り合せ方向は、離型フィルムの幅方向が、偏光フィルムの配向軸と平行となるように行った。
(アクリル粘着剤塗布液)
 アクリル粘着剤(オリバインBPS429-4:東洋インキ製)100部
 硬化剤(BPS8515:東洋インキ製)            3部
 MEK/トルエン混合溶媒(混合比率は1:1)        50部
<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

 実施例2~4:
 実施例1において、ポリエステルフィルム製造時の延伸倍率、フィルム厚さを変更する、ポリビニルアルコールを含む塗布層、シリコーン系離型層の塗布量(乾燥後)、および、離型剤組成の移行成分量を変更する以外は、実施例1と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表1に示す。
Examples 2-4:
In Example 1, the draw ratio at the time of manufacturing the polyester film, the coating thickness that changes the film thickness, the coating amount containing polyvinyl alcohol, the coating amount of the silicone release layer (after drying), and the amount of the migration component of the release agent composition A polyester film was obtained in the same manner as in Example 1 except that the above was changed. The obtained results are summarized in Table 1 below.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

 比較例1:
 離型剤組成を下記のとおり変更する以外は、実施例1と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表2に示す。
 <離型剤組成-B>
 硬化型シリコーン樹脂(KS-847H:信越化学製)     20部
 付加型白金触媒(PL-50T:信越化学製)        0.2部
 MEK/トルエン/n-ヘプタン混合溶媒(混合比率は1:1:1)
 離型剤組成-Bの移行性分量:5重量%
Comparative Example 1:
A polyester film was obtained in the same manner as in Example 1 except that the release agent composition was changed as follows. The results obtained are summarized in Table 2 below.
<Releasing agent composition-B>
Curing type silicone resin (KS-847H: manufactured by Shin-Etsu Chemical Co., Ltd.) 20 parts Addition type platinum catalyst (PL-50T: manufactured by Shin-Etsu Chemical Co., Ltd.) 0.2 part MEK / toluene / n-heptane mixed solvent (mixing ratio is 1: 1: 1 )
Release agent composition-B transferable amount: 5% by weight

 比較例2:
 離型剤組成を下記のとおり変更する以外は、実施例1と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表2に示す。
<離型剤組成-C>
 硬化型シリコーン樹脂(LTC303E:東レ・ダウコーニング製)
                               20部
 シリコーンオイル(KS-64-100cs)       0.18部
 付加型白金触媒(SRX212:東レ・ダウコーニング製)  0.2部
 MEK/トルエン/n-ヘプタン混合溶媒(混合比率は1:1:1)
 離型剤組成-Cの移行性分量:23重量%
Comparative Example 2:
A polyester film was obtained in the same manner as in Example 1 except that the release agent composition was changed as follows. The results obtained are summarized in Table 2 below.
<Releasing agent composition-C>
Curable silicone resin (LTC303E: manufactured by Toray Dow Corning)
20 parts Silicone oil (KS-64-100cs) 0.18 parts Addition type platinum catalyst (SRX212: manufactured by Toray Dow Corning) 0.2 parts MEK / toluene / n-heptane mixed solvent (mixing ratio is 1: 1: 1) )
Release agent composition-C migration amount: 23% by weight

 比較例3:
 実施例1において、<離型組成-A>で、塗布量を0.25g/mに変更する以外は実施例1と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表2に示す。
Comparative Example 3:
A polyester film was obtained in the same manner as in Example 1 except that <mold release composition-A> and the coating amount was changed to 0.25 g / m 2 . The results obtained are summarized in Table 2 below.

 比較例4:
 比較例1において、<離型組成-C>で、塗布量を0.08g/mに変更する以外は比較例1と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表2に示す。
Comparative Example 4:
A polyester film was obtained in the same manner as in Comparative Example 1 except that <Release Composition-C> in Comparative Example 1 and the coating amount was changed to 0.08 g / m 2 . The results obtained are summarized in Table 2 below.

 比較例5~9:
 実施例1において、ポリエステルフィルム製造時のフィルム厚さを変更する、ポリビニルアルコールを含む塗布層、および、シリコーン系離型層の塗布量(乾燥後)を変更する以外は実施例1と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表3に示す。
Comparative Examples 5 to 9:
In Example 1, it changes like the film thickness at the time of polyester film manufacture, It changes like Example 1 except changing the application quantity (after drying) of the coating layer containing polyvinyl alcohol, and a silicone type release layer. Manufactured to obtain a polyester film. The obtained results are summarized in Table 3 below.

 比較例10:
 実施例1において、離型剤組成-Aにシリコーンオイル(AL-1)3部を添加したものを塗布する以外は実施例2と同様にして製造し、ポリエステルフィルムを得た。得られた結果をまとめて下記表3に示す。
Comparative Example 10:
A polyester film was obtained in the same manner as in Example 2 except that the release agent composition A was added with 3 parts of silicone oil (AL-1). The obtained results are summarized in Table 3 below.

Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002

Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003

Claims (5)

 離型層を備えたポリエステルフィルムから成り、離型層を基材レス両面粘着シートの粘着層に張り合わせて使用される離型フィルムであり、離型層が、官能基としてアルケニル基を有するシリコーン樹脂(a)、アルキル基を有するシリコーン樹脂(b)、粘着層への移行成分(c)、及び、白金系触媒(d)を含有し、移行成分(c)の含有量が5~20重量%であるシリコーン系離型層であり、離型層の300mm/分速度域での低速剥離力が10~20mN/cmの範囲であり、かつ、10000mm/分速度域での高速剥離力が低速剥離力の2.5倍以下であることを特徴とする離型フィルム。 Silicone resin consisting of a polyester film having a release layer, which is used by pasting the release layer onto the adhesive layer of a baseless double-sided pressure-sensitive adhesive sheet, and the release layer has an alkenyl group as a functional group (A), containing an alkyl group-containing silicone resin (b), a component (c) for migration to the adhesive layer, and a platinum catalyst (d), and the content of the component (c) for migration is 5 to 20% by weight The release layer is a silicone-based release layer, the release layer has a low-speed peeling force in the range of 300 mm / min. In the range of 10 to 20 mN / cm, and the high-speed peeling force in the range of 10,000 mm / min. A release film characterized by being not more than 2.5 times the force.  ポリエステルフィルムとシリコーン系離型層との間にポリビニルアルコールを含有する塗布液を塗布して得られた塗布層を有する請求項1に記載の離型フィルム。 The release film according to claim 1, further comprising a coating layer obtained by coating a coating liquid containing polyvinyl alcohol between the polyester film and the silicone-based release layer.  シリコーン系離型層中の移行成分が環状シロキサンを含む請求項1又は2に記載の離型フィルム。 The release film according to claim 1 or 2, wherein the migration component in the silicone release layer contains a cyclic siloxane.  シリコーン系離型層の、115°三角錐圧子、0.10mNの試験力でのマルテンス硬度が400N/mm以上である請求項1~3の何れかに記載の離型フィルム。 The release film according to any one of claims 1 to 3, wherein the silicone release layer has a 115 ° triangular pyramid indenter and a Martens hardness of 400 N / mm 2 or more at a test force of 0.10 mN.  ポリエステルフィルムのMOR_C値が1.5~3.0である請求項1~4の何れかに記載の離型フィルム。 The release film according to any one of claims 1 to 4, wherein the polyester film has a MOR_C value of 1.5 to 3.0.
PCT/JP2011/079373 2010-12-27 2011-12-19 Mold release film Ceased WO2012090762A1 (en)

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JP2010289047A JP2012137568A (en) 2010-12-27 2010-12-27 Release polyester film for polarizing plate
JP2010-289047 2010-12-27
JP2011-017375 2011-01-31
JP2011017375A JP2012159548A (en) 2011-01-31 2011-01-31 Mold-release polyester film for polarizing plate
JP2011-026004 2011-02-09
JP2011026004 2011-02-09
JP2011-069055 2011-03-28
JP2011069055A JP2012179888A (en) 2011-02-09 2011-03-28 Polyester film for substrate-less double-sided adhesive sheet

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JP2014205273A (en) * 2013-04-11 2014-10-30 三菱樹脂株式会社 Mold-release polyester film
JP2014226922A (en) * 2013-05-28 2014-12-08 三菱樹脂株式会社 Laminated film
JP2016141446A (en) * 2015-02-03 2016-08-08 三菱樹脂株式会社 Releasable film
JP2016153204A (en) * 2015-02-21 2016-08-25 三菱樹脂株式会社 Release film
JP2016163934A (en) * 2015-03-06 2016-09-08 三菱樹脂株式会社 Release film
JP2016180021A (en) * 2015-03-23 2016-10-13 三菱樹脂株式会社 Substrate-less double-sided adhesive sheet
JP2016187871A (en) * 2015-03-30 2016-11-04 三菱樹脂株式会社 Release film
JP2016188266A (en) * 2015-03-30 2016-11-04 三菱樹脂株式会社 Substrate-less double-sided adhesive sheet
JP2016188265A (en) * 2015-03-30 2016-11-04 三菱樹脂株式会社 Release film

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014205273A (en) * 2013-04-11 2014-10-30 三菱樹脂株式会社 Mold-release polyester film
JP2014226922A (en) * 2013-05-28 2014-12-08 三菱樹脂株式会社 Laminated film
JP2016141446A (en) * 2015-02-03 2016-08-08 三菱樹脂株式会社 Releasable film
JP2016153204A (en) * 2015-02-21 2016-08-25 三菱樹脂株式会社 Release film
JP2016163934A (en) * 2015-03-06 2016-09-08 三菱樹脂株式会社 Release film
JP2016180021A (en) * 2015-03-23 2016-10-13 三菱樹脂株式会社 Substrate-less double-sided adhesive sheet
JP2016187871A (en) * 2015-03-30 2016-11-04 三菱樹脂株式会社 Release film
JP2016188266A (en) * 2015-03-30 2016-11-04 三菱樹脂株式会社 Substrate-less double-sided adhesive sheet
JP2016188265A (en) * 2015-03-30 2016-11-04 三菱樹脂株式会社 Release film

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