WO2004089601A1 - 光学用フィルムの製造法 - Google Patents
光学用フィルムの製造法 Download PDFInfo
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- WO2004089601A1 WO2004089601A1 PCT/JP2004/004351 JP2004004351W WO2004089601A1 WO 2004089601 A1 WO2004089601 A1 WO 2004089601A1 JP 2004004351 W JP2004004351 W JP 2004004351W WO 2004089601 A1 WO2004089601 A1 WO 2004089601A1
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- Prior art keywords
- film
- roll
- support layer
- optical film
- thermoplastic resin
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
- B29C48/915—Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
- B29C48/9155—Pressure rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
- B29C48/914—Cooling of flat articles, e.g. using specially adapted supporting means cooling drums
Definitions
- the present invention relates to a method for producing an optical film, and more particularly, to a method for producing an optical film having small thickness unevenness, excellent smoothness, and uniform optical characteristics over the entire surface.
- Liquid crystal display devices include a polarizing film for generating polarized light, a touch panel with a transparent electrode on the surface, a plastic substrate instead of a glass substrate with a transparent electrode, and a liquid crystal panel generated from liquid crystal molecules.
- a phase difference plate or the like for compensating for the optical phase difference is provided.
- a moisture-resistant protective film is bonded to protect the film from moisture.
- a cast film of triacetyl cellulose is used as such a protective film.
- the evening panel is used by providing a transparent conductive layer on a film substrate, and usually uses a biaxially stretched polyethylene terephthalate film. These films are required to have improved transparency, moisture resistance and birefringence.
- a plastic substrate to replace the glass substrate provided with transparent electrodes.
- various polymer films have been proposed along with the retardation plate described below.
- a stretched optical film is used for the retardation plate.
- Such optical fiber Illum has included polymeric films such as polycarbonate, polysulfone, polyarylate, and polyphenylene sulfide.
- the retardation film is obtained by stretching these polymer films uniaxially or biaxially and orienting them.
- a resin is dissolved in a solvent to form a solution.
- the solution is cast on an endless metal belt or base film, and then the solvent is removed by drying to form a resin layer.
- a method of separating from a metal belt or a base film Japanese Patent Application Laid-Open No. H4-131014.
- the present invention solves the above-mentioned problems of the prior art, and solves the problems of various optical films used in liquid crystal display devices, such as optical films for retardation plates.
- An object of the present invention is to manufacture an optical film having a uniform thickness and substantially no residual retardation, which is useful as a counterpart and has no thickness unevenness such as a die line or a gear mark, and is inexpensive and has high productivity.
- the present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, a cooling roll and a rubber roll made of metal or ceramic together with a support layer of a thermoplastic resin melt-extruded into a film from an extrusion die. It was found that the desired optical film could be obtained by removing the support layer after nipping and transporting in a quasi-adhered state. Further, in producing an optical film by the above method, the present inventors have found an optimal method for pinching the cooling roll and the rubber gap, and have reached the present invention. Disclosure of the invention
- the invention according to claim 1 of the present invention relates to a method of melting and extruding a thermoplastic resin from a die of an extruder into a film, and forming a gap between a cooling roll made of metal or ceramic and a rubber roll that is pressed against and rotated in a circumferential direction of the roll. After the thermoplastic resin layer is transported together with the support layer under cooling tension until the thermoplastic resin layer cools, the support layer is separated and separated.
- a method for producing an optical film characterized in that it is obtained.
- the invention according to claim 2 of the present invention is characterized in that the gap between the cooling roll and the rubber roll is set to any value between 10 and 90% of the total of the thickness of the support layer and the thickness of the film, and Provide a stopper on either the cooling port or the rubber roll so as not to approach the following distance, and apply a pressing force of 2.7 to 10 kgf / cm to the roll on the side where the stopper is provided.
- the manufacturing method of the optical film described in claim 1 is included.
- the invention according to claim 3 of the present invention is characterized in that the support layer is a synthetic resin film.
- the invention according to claim 4 of the present invention is characterized in that the rubber roll has a metal core having a surface hardness.
- the invention according to claim 5 of the present invention is directed to the method for producing an optical film according to any one of claims 1 to 4, wherein the support layer is disposed on a side in contact with the rubber roll to sandwich the thermoplastic resin layer. The content.
- the invention according to claim 6 of the present invention is the method according to any one of claims 1 to 4, wherein the support layer is disposed on both the side in contact with the rubber roll and the side in contact with the cooling roll to sandwich the thermoplastic resin layer.
- the support layer is disposed on both the side in contact with the rubber roll and the side in contact with the cooling roll to sandwich the thermoplastic resin layer.
- the invention according to claim 7 of the present invention includes the method for producing an optical film according to any one of claims 1 to 6, wherein the thermoplastic resin is a cyclic polyolefin.
- the invention according to claim 8 of the present invention includes the method for producing an optical film according to any one of claims 1 to 7, wherein the support layer is made of biaxially stretched polyethylene terephthalate.
- the invention according to claim 9 of the present invention is obtained by the production method according to any one of claims 1 to 8, and has a smoothness of 0.01 ⁇ m or less in average roughness Ra,
- the method for producing an optical film according to any one of claims 1 to 8, comprising obtaining an optical film having a refractive index of 30 nm or less in a retardation.
- the invention according to claim 10 of the present invention is characterized in that the retardation is 2 O nm or less, and the transmitted light of the light incident on the film in the direction of 45 degrees is projected on a vertical surface to produce a light and shade. 9. A method according to claim 1, wherein an optical film in which stripes or patterns are substantially invisible is obtained.
- FIG. 1 is a schematic diagram in the case where the optical film of the present invention is manufactured by disposing a single-sided support layer and pressing it.
- FIG. 2 is a schematic diagram of a case where the optical film of the present invention is manufactured by disposing a double-sided support layer and pressing it.
- FIG. 3 is a schematic view showing a structure of a stopper (a set of rollers) for setting a gap between a cooling roll and a rubber roll according to the present invention.
- (a) is a top view
- (b) is a side view
- (c) is a schematic diagram showing a state when a gap is set.
- FIG. 4 is a schematic diagram for observing optical unevenness of a product film.
- the resin flow due to the shearing of the die line and the melt extruded resin generated from the extrusion die and the film shrinking and taking off the resin due to cooling, even after various refinements and improvements.
- a residual phase difference occurs due to the stress applied.
- a smooth surface is usually captured by pressing between a metal roll and a metal roll or a smooth metal belt, and furthermore, the resin flow in the extrusion direction and the thickness unevenness of the resin in the extrusion direction such as a die line. Attempts have been made to eliminate this by causing the resin to flow in other directions due to pressure.
- the present inventors used a cooling roll made of a hard material, that is, a metal or ceramics, and a roll made of a soft material, that is, a rubber roll, and formed a support layer made of a synthetic resin film or the like that is a poor conductor of heat.
- a cooling roll made of a hard material that is, a metal or ceramics
- a roll made of a soft material that is, a rubber roll
- formed a support layer made of a synthetic resin film or the like that is a poor conductor of heat By pressing the molten extruded resin layer through the gap, the adhesion and adhesion between the support layer and the extruded resin are strengthened more than in the case of metal-to-metal clamping, and the pressure distribution by the rubber roll is caused, and the molten resin from the die Even if the thickness unevenness occurs, the other person It has been found that the resin flow is easy to flow in the direction, and the surface is flattened. The smooth surface is well copied, and the residual
- the support layer made of a synthetic resin film or the like which is a poor heat conductor, has heat insulation properties, becomes softer as the temperature rises, and becomes more compatible with the molten resin. This is probably because the bite is smoother than metal. Furthermore, when a support layer is used, the temperature gradient in the thickness direction of the molten resin is reduced, and distortion of the front and back of the product film is unlikely to occur.
- melt-extruded resin layer is transported together with the support layer until the temperature reaches an appropriate temperature, shrinkage due to cooling and stress of taking over can be avoided from being applied to the target optical film. It is considered that the uneven phase and the residual phase difference generated by the manufacturing process can be eliminated at the same time.
- thermoplastic resin used in the present invention a resin suitable for producing an optical film is selected. To this end, it must be a transparent resin, and must have sufficient heat resistance and humidity resistance to be practically acceptable, for example, in order to increase the reliability of the embedded liquid crystal display during use. Is required.
- a thermoplastic resin polycarbonate, polysulfone, polyarylate, aromatic polyester, cyclic polyolefin and the like are preferable. Among them, cyclic polyolefins have low moisture absorption, high heat resistance, and excellent optical properties compared to other thermoplastic resins.Especially, birefringence due to molecular orientation is less likely to occur when molecules are oriented. Suitable for producing raw film.
- the cyclic polyolefin has an alicyclic structure in a main chain and / or a side chain.
- the alicyclic structure include a cycloalkane structure and a cycloargen structure, and a cycloalkane structure is suitable for optical use.
- the unit of these alicyclic structures preferably has 5 to 15 carbon atoms.
- a polymer containing 50% by weight or more of these units having an alicyclic structure is preferable. Examples of such a polymer include a norbornene-based polymer, a monocyclic cyclic olefin-based polymer, a cyclic conjugated gen-based polymer, a hydrocarbon polymer having a side chain alicyclic structure, and hydrogenated products thereof.
- a norbornene-based polymer and its hydrogenated product a cyclic conjugated-gen-based polymer and its hydrogenated product are preferable.
- Typical resins are ARTON (trade name of JSR Corporation), ZONEX (trade name of Zeon Corporation), Zeonor (trade name of Zeon Corporation), Abel (trade name of Mitsui Chemicals Corporation) ) And the like.
- FIG. 1 is a schematic diagram for explaining the melt extrusion molding method in the present invention.
- the extruder may be a single-screw, twin-screw or melt kneader.
- the shape of each screw is appropriately selected and is not particularly limited.
- the screw diameter is 40 ⁇ 150
- L / D is 20-38.
- the compression ratio is 2.5 ⁇ 4.
- the extrusion die 1 may have a usual shape used for forming a sheet or a film.
- a coat hanger type, a straight manifold type, and a fish tail type die can be used.
- the gap between the openings of the extrusion die 1 is selected according to the thickness of the target sheet or film, but is usually about 0.1 to 3 mm.
- a film-like molten resin 8 extruded from an extrusion die 1 is sandwiched between a support layer 9 sandwiched between a cooling roll 2 made of metal or ceramic and a rubber roll 3.
- the rubber roll 3 is pressed against the cooling roll 2 by a metal backup roll 4 to apply a uniform pressure to the entire width of the molten resin 8, and a gap with the cooling roll is set.
- the metal of the roll material is not particularly limited, and for example, a known material such as iron and stainless steel is used.
- two stoppers 13 having the same gradient which is called “copper” are used. That is, one stopper 13 b is provided on the rotating shaft of the cooling roll 2 or the rubber roll 3 (the rubber roll 3 in the figure), the other stopper 13 a is provided on the rail 14, and Slide to desired position Fixed to.
- the stoppers 13a and 13b can vertically adjust the gap W between the cooling roll 2 and the rubber roll 3 by sliding the inclined surfaces facing each other up and down. Further, the stoppers 13a and 13b can prevent the gap W between the cooling roll 2 and the rubber port 3 from approaching a certain value or more. Then, it is pressed down by the set pressing force through the backup roll 4 so that the set gap W is maintained.
- the set pressing force is transmitted to the backup roll 4 by an air cylinder (not shown) through the air pressure.
- the temperature of the cooling roll 2 is precisely controlled, and usually a temperature in the range of + 30 ° C. to —70 ° C. starting from the glass transition temperature of the molten resin 8 is appropriate.
- the molten resin 8 is conveyed to the second cooling roll 5 in a state of being quasi-adhered to the support layer 9 while being sandwiched between the cooling roll 2 and the support layer 9, and is conveyed to the second cooling roll 5 under a constant tension. , And cooled to form a molded film 11.
- the forming film 11 and the support layer 9 are taken off from the second cooling port 5 with the take-off force adjusted by the third cooling roll 6 in a pseudo-adhered state, and the support layer 9 is separated and separated here.
- the film 11 is sent via a roll 7 as a film product 12 to a take-up reel (not shown) and wound up. Each of the rolls is driven so that the support layer 9 and the molten resin 8 or the molded film 11 are conveyed together in conjunction or independently.
- FIG. 2 is a schematic diagram of a case where the support layers 9 and 10 are arranged on both sides of the film-like molten resin 8, that is, on both the side in contact with the rubber roll 3 and the side in contact with the cooling roll 2.
- the operation is almost the same as that of the support layer on one side in Fig. 1, including the temperature condition of the cooling roll.
- the respective support layers 9 and 10 are separated and separated by the cooling rolls 6 and 7 and wound up as a film product 12. It is important that the support layer to be pinched is a poor conductor of heat as compared with metals and ceramics, and a synthetic resin film is preferable.
- a support layer having a surface as flat and as few as possible with irregularities is preferred, and is defined in JISB 0601.
- a support layer having a surface roughness characteristic of less than 0.01 m in center line average roughness is preferred.
- a synthetic resin film as a support layer it must be resistant to a molten resin extruded into a film.
- films having relatively high heat resistance such as polycarbonate, polysulfone, polyethersulfone, polyphenylsulfide, and polyimide, biaxially oriented polyethylene terephthalate, biaxially oriented polyethylene naphthalate, and other biaxially oriented films, And the like.
- a film made of the above resin obtained by casting with a solvent, a casting film of triacetyl cellulose, and a biaxially stretched polyester film are preferable. Then, the molten resin extruded into a film and the support layer are conveyed together while being pressed.
- the extruded (melted) resin and the support layer may be of the same type or different types as long as they can be quasi-adhered or separated after cooling.
- the rubber roll used for pinching preferably has a structure in which various rubber-like substances are concentrically wound around a metal core.
- the thickness of the rubber-like substance is appropriately selected, but is preferably 5 to 15 mm. When the thickness of the rubber-like substance is less than 5 mm, it is close to that of a metal alone, and the pinching effect is small.On the other hand, when the thickness exceeds 15 mm, the rubber is greatly deformed and wrinkles of the support layer are generated. I'm sorry.
- the hardness of the rubber-like substance has an effect on the effect of pinching pressure. If the Shore hardness is less than 60, the effect of flattening the thickness unevenness of the molten resin from the die is small and the residual retardation is large.
- Shore hardness is The presence of 100 or more rubber rolls is small.
- NBR is usually used for laminating the thermoplastic resin and the support layer.SBR, chloroprene, chlorinated polyethylene, chlorosulfonated polyethylene, polyester elastomer, urethane dam, silicon rubber, etc. It can be selected from these compounds. NBR or silicon rubber is preferred from the viewpoint of operating temperature.
- Optical unevenness of the optical film includes die lines along the film production direction, vertical stripes such as thick and thin unevenness, horizontal stripes due to gear marks perpendicular to this line, and insufficient adhesion between the film cooling port and the support layer. There are three types of adhesion unevenness.
- the pressing force of the rubber roll or the cooling roll on the opposing pressing side becomes excessive, vertical stripes are easily eliminated, but horizontal stripes are easily generated.
- the pressing force is preferably in the range of 2.7 to 10 kgf / cm, and more preferably in the range of 3.0 to 7.0 kgf / cm.
- the linear pressure in this appropriate range has a characteristic that is extremely lower than the linear pressure used for a laminated product of synthetic resins produced by ordinary pinching, resin lamination to paper, and the like.
- the gap between the rubber roll and the cooling roll is not usually set (substantially no gap), and even if it is set, it is optional.
- the setting of the gap is important. Therefore, the set value of the gap is preferably set within a range of 10 to 90% of the sum of the thickness of the support layer sandwiched at the same time and the thickness of the obtained thermoplastic film. If the gap ratio is less than 10%, a bank of molten resin is formed in the gap between the cooling roll and the rubber roll, so that a gear mark is easily formed. On the other hand, if it exceeds 90%, it becomes difficult to eliminate vertical stripes Not only that, but also the birefringence tends to increase. More preferably, it is 40 to 60%.
- the thickness of the support layer is not limited. However, if the thickness is too small, the effect is small. If the thickness is too large, the operation is likely to be hindered. Therefore, usually 50 to 200 m is preferred.
- the support layer can be supplied by being preheated before being pressed with the molten resin.
- the temperature is a temperature above the cooling temperature of the operation and at which the support layer does not undergo thermal contraction.
- the support layer and the molten resin layer are conveyed together until cooled, separated and separated. If the two are of different types, it may be difficult to transport them together due to insufficient adhesion.
- the laminating surface is treated with corona discharge and ozone to increase the adhesion of the support layer. It is preferable to increase the adhesive strength by performing a surface treatment such as a flame treatment, a glow discharge and a plasma discharge treatment.
- a film having no die line and having a uniform film thickness is required.
- the difference between the maximum and the minimum of the film thickness is preferably 5% or less of the average film thickness, more preferably 2% or less.
- the surface roughness of the film is preferably not more than 0.01 ⁇ m in terms of center line average roughness Ra based on JIS B 0601. Eliminating the die line is to reduce the amount of foreign matter by passing the molten resin through an appropriate filter material, and to reduce the die line from the die by setting extrusion conditions that minimize the generation of burnt resin.
- smoothness can be achieved by strictly adjusting the die gap and optimizing the operating conditions for pressing the support layer and the support layer as described above.
- optical unevenness is roughly divided Vertical stripes, horizontal stripes, and uneven adhesion are observed. Even if these optical irregularities are not observed with ordinary transmitted light, they can be confirmed very well by obliquely entering the light and projecting the transmitted light on a vertical surface for observation. Increasing the angle of the oblique direction makes it easier to observe, but it is practically not hindered unless it is normally visible at 45 degrees incidence.
- optical unevenness is more easily observed when the light source of the transmitted light to be incident is brighter, and is more visible when the light and shade of the stripe pattern is oblique to the incident light.
- a low birefringence film having almost no variation is required as an extruded film used as a raw material of various optical films.
- This variation is preferably 5 nm or less when the retardation is expressed in nm, and it is more advantageous to achieve a smaller retardation of the film to achieve this.
- the film thickness is 100 m, It is preferably at most 3 O nm, more preferably at most 2 O nm, even more preferably at most 10 nm.
- Such a film having a small variation can be sufficiently achieved by pressure-molding with a support layer using a cyclic polyolefin having a small photoelastic coefficient which does not easily generate birefringence during molecular orientation.
- the optical film obtained as described above can be used as a moisture-resistant protective film of a positively-adsorbed and stretched polyvinyl alcohol polarizing film by bonding it to various pressure-sensitive adhesives or adhesives.
- touch panels with a transparent conductive layer on the surface and plastic substrates that replace glass substrates for liquid crystal displays use metal oxide films, such as ITO (indium tin monoxide) films and AZO (aluminum-doped zinc oxide) films.
- ITO indium tin monoxide
- AZO aluminum-doped zinc oxide
- the above-mentioned optical film is used as a raw material for the retardation plate, and after preheating, the film is stretched at a constant temperature between two rolls having different peripheral speeds in the same direction as the winding direction of the film. Thereby, a retardation film of the longitudinal stretching can be obtained.
- a raw optical film is gripped on both sides of the film with clamps or pins and stretched in the direction perpendicular to the running direction while running, whereby a retardation film stretched in the transverse direction can be obtained.
- a simultaneous biaxially stretched film is obtained, and a retardation film in the thickness direction is obtained.
- the film After stretching in the longitudinal or transverse direction, the film can be further stretched in two directions in either direction.
- the stretching ratio is usually 1.5 to 4 times. Instead of stretching, the stretching effect can also be obtained by rolling between rolls that does not shrink in the film width direction.
- the obtained stretched optical film is useful as various optical films.
- a cyclic polyolefin resin (Aton D4531, Tg1332 ° C, manufactured by JSR Corporation) was placed on the schematic diagram of FIG. After passing through the porous filler through the shaft screw, it was extruded into a film from the extrusion die 1 with a width of 884 I at a constant discharge rate by a gear pump. As the extrusion die 1, a chalkless coat hanger die was used. The temperature of the molten resin 11 discharged from the extrusion die 1 was 278 ° C.
- the support layer 9 has a thickness of 75 m, and has a surface roughness characteristic of 0.05 in center line average roughness Ra, 0.07 m in maximum roughness R max, and 10 point flatness.
- a biaxially stretched polyethylene terephthalate film (03 LF 8, Teijin Dupont Film Co., Ltd.) with an average roughness Rz of 0.07 m is placed on the rubber roll 3 side, and the film-like molten resin is applied with a surface pressure of 12 kgf. pressure m 2 clamping between the metal cooling roll 2 by (air one cylinder pressure 1 3 kgf / cm 2 below in example 6, a rubber roll contact surface length 8 mm, linear pressure 9. corresponding to 5 kgf / cm) O Cooling roll 2 was maintained at 90 ° C.
- the support layer 9 and the molten resin layer 8 are both transported to a second cooling roll 5 kept at 47 ° C, and then transported to a third cooling roll 6 kept at 35 ° C.
- the polyethylene terephthalate film of the support layer 9 was separated and wound up.
- the formed film 11 was wound up as a film product 1 through the next roll 7.
- the speed of the operation line was 6 m / min.
- Parallel light from a halogen lamp of 100 W is incident on the sample film surface placed obliquely with the film flowing direction up, and the transmitted light is projected onto a screen to check the linear density of the light.
- the film thickness was measured at 35 locations at intervals of 2 Omm in the width direction of the sample film using a film thickness meter to determine the average value, and the maximum and minimum tolerances were determined.
- Automatic birefringence meter KOBRA- 21 ADH, Nicol polarizer and Nicol analyzer are placed in parallel with each other, and the sample film is irradiated with a single-wavelength light beam, and the angle dependence of the transmitted light intensity when it makes one rotation around the beam axis.
- the phase difference is calculated from the characteristics.
- Example 1 Except that the thickness of the biaxially stretched polyethylene terephthalate as the support layer was changed from 75 m in Example 1 to 125 m, a molded film 11 (film) was produced in the same manner as in Example 1. Product 12) was manufactured and various properties were measured. The results are shown in Table 1.
- Example 1 Same as Example 1 except that one support layer 9 was provided on the rubber roll 3 side, the other support layer 10 was also provided on the cooling roll 2 side, and the molten resin layer 8 was pressed from both sides.
- a molded film 11 (film product 1 2) was obtained by the above method and various properties were measured. The results are shown in Table 1.
- Example 1 Same as Example 1 except that the speed of the operation line of Example 1 was changed to 12 m / min, and the discharge amount corresponding to this was extruded so that the film thickness was almost the same as that of Example 1. Molded film 11 (film product 1 2) was obtained by the method described above. Table 1 shows the properties of this film.
- Example 1 a polycarbonate (panlite L122-ZE, Tg145 ° C, manufactured by Teijin Limited) was used as a film-like molten resin layer by the same apparatus as in Example 1. 8 was extruded. The extruded resin temperature was 280 ° C.
- Table 2 also shows the characteristic values of the solution cast polycarbonate film used in Example 5.
- Example 5 Example 2 Female removal Single-sided ⁇ Main layer ⁇ Cast ⁇ inolem Support ⁇ Main layer () Night cast film
- Example 2 The same method as in Example 1 was used, except that the temperature of the molten resin 8 discharged from the extrusion die 1 was 267 ° C.
- the support layer 9 has a thickness of 115 m, a surface roughness characteristic defined in JISB 0601 of center line average roughness Ra of 0.05 im, and a maximum roughness Rmax of 0.
- a biaxially stretched polyethylene terephthalate film (03 LF 8, manufactured by Teijin Dupont Film Co., Ltd.) with a thickness of 0.07 im and an average roughness of 10 points Rz of 0.07 im was placed on the rubber roll 3 side, and 90 ° Between a metal (steel) cooling roll 2 held at C and a metal (steel) core with a 6.5 mm thick Sure-hardness 90 NBR 85 5 mm Omm long rubber roll 3 Pressure.
- the ratio of the gap between the cooling roll and the rubber roll to the total thickness of the support and the product film is 48.9%. [110 urn / (125 um + 100 um) xl 00].
- the pressing force of the rubber roll 3 through Roh click up roll 4 so pressed the roles across a cooling roll side by radial 3. 1 5 cm air one cylinder 2 group using air pressure 5Kgf7cm 2, the rubber roll line pressure Is 3.67 kg f / cm. (Cooling and film winding method)
- the surface roughness characteristics of the obtained molded film 11 were almost similar to those of the support layer.
- the measurement of the film thickness and the retardation was performed in the same manner as in Example 1.
- the characteristics of optical unevenness were observed and measured by the following methods. Table 3 shows the results.
- the illuminance was greatly increased compared to the case of Examples 1 to 6, and the evaluation of vertical stripes and horizontal stripes was clarified for the rays from the point light source of the xenon lamp of 15 to observe the vertical stripes
- the direction of flow of the film product 12 is set, light is incident from the 45 degree direction of the product, and the transmitted light is projected on the screen 16 behind and observed.
- the evaluation of observation results is based on the following criteria.
- a film was prepared in the same manner as in Example 6 except that the gap ratio between the cooling roll and the rubber roll was set to 13.3%, and the characteristic values and the like are shown in Table 3.
- a film was prepared in the same manner as in Example 6 except that the gap ratio between the cooling roll and the rubber roll was set to 88.9%, and the characteristic values and the like are shown in Table 3. Was.
- a film was prepared in the same manner as in Example 6 except that the gap ratio between the cooling roll and the rubber roll was set to 0% (in a state where the cooling roll and the rubber roll were in contact with each other) (Example 9). was set to 100% (2 25 im of the sum of the thickness of the support layer 12.5.m and the thickness of the product film 100 m), and a film was prepared in the same manner as in Example 1 ( Table 10 shows the characteristic values and the like of Example 10) and the obtained films.
- Example 6 Example 7
- Example 8 Example 9
- Example 10 Chilled alcohol and rubber mouth 110 30 200 0
- the gap between the cooling roll and the rubber roll has an appropriate range to minimize optical unevenness. That is, when the gap ratio is in the range of 10 to 90%, an excellent film having less variation in film thickness and variation in retardation can be obtained.
- Example 11 Example 12
- Example 13 Example 14 Gap (m) Gap Ratio (%) 48.9 48.9 48.9 48.9 Pressing Force (Pressurized Air Pressure) 8 12 3 20
- Adhesion unevenness 3 3 1 3 From Tables 4 and 3, it can be seen that a film having less variation in film thickness and retardation and less optical unevenness can be obtained under an appropriate pressing force. That is, when the pressing force is in the range of 2.7 to 10.0 kgf / cm, an excellent film with less variation in film thickness and variation in retardation and further less optical unevenness can be obtained. Industrial applicability
- the method of the present invention in which a resin melt-extruded into a film is pressed together with a support layer of a heat-defective conductor between hard and soft rolls, that is, between a metal or ceramic roll and a rubber roll, is formed by using a die line.
- a gap between the rolls is determined to be between 10% and 90% of the total of the thickness of the support layer and the thickness of the film, and a stopper is provided on one of the rolls so as not to be closer than this distance.
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US10/552,478 US20060237864A1 (en) | 2003-04-10 | 2004-03-26 | Method for producing optical film |
Applications Claiming Priority (4)
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JP2003106433A JP3920805B2 (ja) | 2003-04-10 | 2003-04-10 | 光学用フィルムの製造法 |
JP2003-106433 | 2003-04-10 | ||
JP2003407336A JP3920842B2 (ja) | 2003-12-05 | 2003-12-05 | 光学用フィルムの製造方法 |
JP2003-407336 | 2003-12-05 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110091528A (zh) * | 2018-01-29 | 2019-08-06 | 上海龙驭塑业有限公司 | 一种pvc硬软质片膜通用型五辊压延生产线 |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7833588B2 (en) * | 2002-12-20 | 2010-11-16 | Teijin Limited | Transparent conductive laminate, touch panel and touch panel-equipped liquid crystal display |
JP4764705B2 (ja) * | 2005-11-22 | 2011-09-07 | 富士フイルム株式会社 | 熱可塑性樹脂フィルムの製造方法 |
KR100823127B1 (ko) * | 2005-12-31 | 2008-04-21 | 정영진 | 캐스팅 필름 및 그 제조방법 |
US20090239001A1 (en) * | 2006-07-19 | 2009-09-24 | Konica Minolta Opto, Inc. | Optical film and method for production thereof |
US8864929B2 (en) * | 2006-10-31 | 2014-10-21 | Dexerials Corporation | Method for manufacturing laminated soft-magnetic sheet |
JP5174595B2 (ja) * | 2007-09-21 | 2013-04-03 | 住友化学株式会社 | ポリプロピレン系樹脂製位相差フィルム用原反フィルムの製造方法 |
US20140264979A1 (en) * | 2013-03-13 | 2014-09-18 | Transitions Opticals, Inc. | Method of preparing photochromic-dichroic films having reduced optical distortion |
KR101459065B1 (ko) * | 2014-05-16 | 2014-11-12 | 에스맥 (주) | 터치 스크린 패널 제작용 라미네이션 장치 |
EP3332941B1 (en) * | 2015-08-04 | 2021-10-13 | AGC Inc. | Method for producing fluororesin film |
CN106042590A (zh) * | 2016-07-21 | 2016-10-26 | 上海市凌桥环保设备厂有限公司 | 一种具有温度补偿功能的高温复合机 |
CN111124169B (zh) * | 2018-10-31 | 2023-08-29 | 瀚宇彩晶股份有限公司 | 触控显示装置 |
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JPH09239812A (ja) * | 1996-03-08 | 1997-09-16 | Sekisui Chem Co Ltd | 光学フィルムの製造方法及び光学フィルム |
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CA1319857C (en) * | 1988-07-26 | 1993-07-06 | Kiyoshi Hirota | Image transfer apparatus |
KR0167860B1 (ko) * | 1995-10-23 | 1999-01-15 | 히로세 준고 | 광학기능의 연속시트 |
KR100454801B1 (ko) * | 1996-06-26 | 2005-01-17 | 이데미쓰세끼유가가꾸가부시끼가이샤 | 엠보싱패턴가공방법,그의가공장치및엠보싱시이트 |
DE60229190D1 (de) * | 2001-08-10 | 2008-11-20 | Sekisui Chemical Co Ltd | Optische Kunststofffolie, Verfahren zu deren Herstellung und Polarisator |
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2004
- 2004-03-26 WO PCT/JP2004/004351 patent/WO2004089601A1/ja active Application Filing
- 2004-03-26 KR KR1020057019172A patent/KR100694281B1/ko active IP Right Grant
- 2004-03-26 US US10/552,478 patent/US20060237864A1/en not_active Abandoned
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JPH06170919A (ja) * | 1992-12-10 | 1994-06-21 | Aipetsuku:Kk | 熱可塑性樹脂シート又はフイルムの製造方法及びその装置 |
JPH09239812A (ja) * | 1996-03-08 | 1997-09-16 | Sekisui Chem Co Ltd | 光学フィルムの製造方法及び光学フィルム |
JPH1010321A (ja) * | 1996-06-27 | 1998-01-16 | Sekisui Chem Co Ltd | 光学フィルム及びその製造方法 |
JPH1016034A (ja) * | 1996-07-01 | 1998-01-20 | Sekisui Chem Co Ltd | 光学フィルムの製造方法 |
JP2000280315A (ja) * | 1999-04-01 | 2000-10-10 | Nippon Zeon Co Ltd | 環状オレフィン樹脂製押出成形物及びその製造方法 |
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CN110091528A (zh) * | 2018-01-29 | 2019-08-06 | 上海龙驭塑业有限公司 | 一种pvc硬软质片膜通用型五辊压延生产线 |
Also Published As
Publication number | Publication date |
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US20060237864A1 (en) | 2006-10-26 |
KR100694281B1 (ko) | 2007-03-14 |
KR20050121255A (ko) | 2005-12-26 |
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