WO2018142983A1 - Biaxially oriented polypropylene-based film - Google Patents
Biaxially oriented polypropylene-based film Download PDFInfo
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- WO2018142983A1 WO2018142983A1 PCT/JP2018/001767 JP2018001767W WO2018142983A1 WO 2018142983 A1 WO2018142983 A1 WO 2018142983A1 JP 2018001767 W JP2018001767 W JP 2018001767W WO 2018142983 A1 WO2018142983 A1 WO 2018142983A1
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- film
- layer
- base material
- biaxially oriented
- material layer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/50—Properties of the layers or laminate having particular mechanical properties
- B32B2307/514—Oriented
- B32B2307/518—Oriented bi-axially
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2323/00—Polyalkenes
- B32B2323/10—Polypropylene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
Definitions
- the present invention relates to a biaxially oriented polypropylene film. Specifically, the present invention relates to a biaxially stretched polypropylene film having excellent adhesion to printing ink and adhesion to an adhesive used for laminating with other member films.
- biaxially oriented polypropylene-based films are widely used as packaging materials for various articles such as foods and textile products because of their excellent transparency and mechanical properties.
- polypropylene film for example, since polypropylene resin is nonpolar, the surface energy is small, and therefore, the adhesiveness with printing ink or other materials is not sufficient in processing of printing ink or laminate, etc. It has been pointed out that there is no.
- a biaxially oriented polypropylene film when used as a packaging material, it is generally performed to laminate with another member film using an adhesive, but the laminate strength between these films is weak. In some cases, the strength of the packaging material is weakened and it breaks and the contents protrude, and oxygen and water vapor enter and exit through the torn part of the bag, so that it does not serve as a food packaging material. As mentioned.
- biaxially oriented polypropylene film is generally printed, but from the viewpoint of color development and color fading, printing from the ink printing roll to the surface of the biaxially oriented polypropylene film. Improvements in ink transferability and adhesion of printing ink to the film surface are more demanded.
- a skin layer composed of a composition in which organic polymer fine particles are blended with a propylene-ethylene random copolymer is formed on the surface of a biaxially oriented polypropylene film.
- a laminated film is disclosed (for example, see Patent Document 1), not only the adhesion of the printing ink is insufficient, but also a process of separately providing a skin layer is required, resulting in poor productivity.
- the present invention does not impair the excellent transparency and mechanical properties inherent in the biaxially oriented polypropylene film, has a high lamination strength with other member films, and transfers printing ink from the printing roll to the film. It is an object to provide a biaxially oriented polypropylene film having excellent properties and adhesion of printing ink.
- the present invention that has solved the above problems is a surface layer (B) having a polypropylene resin as a main component on at least one surface of a base material layer (A) having a polypropylene resin as a main component and a substrate layer (A).
- the surface roughness of the surface of the surface layer (B) opposite to the substrate layer (A) is 0.027 ⁇ m or more and 0.040 ⁇ m or less, and the substrate layer of the surface layer (B)
- the surface resistivity of the surface opposite to (A) is 15 Log ⁇ or more
- the wetting tension of the surface of the surface layer (B) opposite to the base material layer (A) is 38 mN / m or more
- the film The biaxially oriented polypropylene film is characterized in that the thickness is 20 ⁇ m or more and 50 ⁇ m or less, and the haze (transparency) value of the film is 5% or less.
- center surface peak height SRp + center surface valley depth of the surface of the surface layer (B) opposite to the base material layer (A) is 1.0 ⁇ m or more and 2.0 ⁇ m or less.
- the heat shrinkage rate at 150 ° C. in the longitudinal direction and the transverse direction of the biaxially oriented polypropylene film is 11% or less.
- a laminate having a printing layer on the side opposite to the substrate layer of the surface layer (B) of the biaxially oriented polypropylene film described in any one of the above is preferable.
- the biaxially oriented polypropylene film of the present invention has a large laminate strength with other member films without impairing the excellent transparency and mechanical properties inherent to the biaxially oriented polypropylene film, and a printing roll
- the film is excellent in transferability of printing ink from film to film and adhesion of printing ink, and can be produced efficiently.
- the biaxially oriented polypropylene film of the present invention has a surface layer (B) containing a polypropylene resin as a main component on at least one surface of a base material layer (A) and a base material layer (A) containing a polypropylene resin as a main component.
- the arithmetic average roughness of the surface of the surface layer (B) opposite to the substrate layer (A) is 0.027 ⁇ m or more and 0.040 ⁇ m or less, and the substrate of the surface layer (B)
- the surface resistivity of the surface opposite to the layer (A) is 15 Log ⁇ or more, and the wetting tension of the surface of the surface layer (B) opposite to the base material layer (A) is 38 mN / m or more
- the film thickness is 20 ⁇ m or more and 50 ⁇ m or less, and the haze value of the film is 5% or less.
- the arithmetic surface roughness SRa of the surface layer (B) opposite to the base material layer (A) is measured in the X direction using a three-dimensional roughness meter at a stylus pressure of 20 mg.
- the length of 1 mm, the feed pitch in the Y direction is 2 ⁇ m, the number of recorded lines is 99, the height direction magnification is 20000 times, and the cutoff is 80 ⁇ m.
- arithmetic mean roughness described in JISB 0601 (1994) It is.
- Arithmetic average roughness SRa is not easily affected by one protruding large peak or valley, and is relatively small formed on a surface other than a relatively large peak or valley formed locally by an antiblocking agent or lubricant. It becomes an index that represents uneven undulations. Since most of the printing ink adheres to the surface other than the relatively large peaks and valleys formed by the antiblocking agent or lubricant, it has a great relationship with the adhesion of the printing ink. This is different from the center plane mountain height SRp and the center plane valley depth SRv described later. Further, the surface specific resistance value of the surface layer (B) opposite to the base material layer (A) is different from the amount of the antistatic agent present on the surface, and the antistatic material existing on the surface.
- the surface resistance value increases as the amount of the agent decreases.
- the wetting tension of the surface layer (B) represents the numerical value of the surface tension ( ⁇ N / cm) of the mixed solution reagent determined to wet the film surface, and is related to the wettability of the printing ink and the adhesive. . Further details will be described below.
- the polypropylene resin used for the base layer (A) of the biaxially oriented polypropylene film of the present invention is a propylene polymer or propylene and ethylene and / or an ⁇ -olefin having 4 or more carbon atoms of 0.5 mol% or less.
- the copolymer component in the copolymer is preferably 0.3 mol% or less, more preferably 0.1 mol% or less, and most preferably complete homopolypropylene containing no copolymer component.
- the mesopentad fraction ([mmmm]%) measured by 13C-NMR which is an index of stereoregularity of the polypropylene resin constituting the base material layer (A) of the biaxially oriented polypropylene film of the present invention, is 98 to It is preferable that it is 99.5%. More preferably, it is 98.1% or more, More preferably, it is 98.2% or more. When the mesopentad ratio of the polypropylene resin is small, the elastic modulus is low and the heat resistance may be insufficient. 99.5% is a realistic upper limit.
- the mass average molecular weight (Mw) of the polypropylene resin constituting the substrate layer (A) of the biaxially oriented polypropylene film of the present invention is preferably 180,000 to 500,000. If it is less than 180,000, the melt viscosity is low, so that it is not stable at the time of casting, and the film-forming property may deteriorate. When Mw exceeds 500,000, the amount of the component having a molecular weight of 100,000 or less becomes 35% by mass, and the heat shrinkage rate at high temperature is reduced.
- the lower limit of Mw is more preferably 190,000, still more preferably 200,000, and the upper limit of more preferable Mw is 320,000, more preferably 300,000, particularly preferably 250,000.
- the number average molecular weight (Mn) of the polypropylene resin constituting the base layer (A) of the biaxially oriented polypropylene film of the present invention is preferably 20,000 to 200,000. If it is less than 20,000, the melt viscosity is low, so that it is not stable at the time of casting, and the film-forming property may deteriorate. When it exceeds 200,000, the thermal shrinkage rate at a high temperature is reduced.
- the lower limit of Mn is more preferably 30,000, more preferably 40,000, particularly preferably 50,000, and the upper limit of Mn is more preferably 80,000, still more preferably 70,000, particularly preferably 60,000. is there.
- Mw / Mn is preferably in the range of 5.5 to 20 or less.
- Mw / Mn which is an index of molecular weight distribution, is preferably 2.8 to 8 in the polypropylene resin of the base material layer (A). More preferably, it is 2.8 to 7, more preferably 2.8 to 6, and particularly preferably 2.8 to 5.4. Further, the lower limit is preferably 3 or more, and more preferably 3.3 or more.
- the molecular weight distribution of polypropylene resin is determined by polymerizing different molecular weight components in a series of plants in multiple stages, blending different molecular weight components offline in a kneader, or blending catalysts with different performance. It can be adjusted by polymerizing or using a catalyst capable of realizing a desired molecular weight distribution.
- the polypropylene resin of the base layer (A) of the biaxially oriented polypropylene film of the present invention has a melt flow rate (MFR: 230 ° C., 2. 16 kgf) is preferably from 4 g / 10 min to 20 g / 10 min.
- MFR melt flow rate
- the lower limit of the MFR of the polypropylene resin of the base material layer (A) is more preferably 5 g / 10 minutes, further preferably 6 g / 10 minutes, and particularly preferably 7 g / 10 minutes.
- the upper limit of the MFR of the polypropylene resin of the base material layer (A) is more preferably 15 g / 10 minutes, and further preferably 12 g / 10 minutes.
- the Mw / Mn and MFR of the polypropylene resin of the base material layer (A) are within this range, the heat shrinkage rate at high temperatures can be kept small, and the film has good adhesion to the cooling roll. Excellent in properties.
- the surface roughness of the surface layer (B) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is 0.027 ⁇ m or more and 0.040 ⁇ m or less. If it is less than 0.027 ⁇ m, the adhesion to the printing ink and the laminate strength with other member films are not sufficient, and if it exceeds 0.040 ⁇ m, the haze increases or the color developability of printing deteriorates. Occurs.
- the surface roughness of the surface layer (B) opposite to the base material layer (A) is more preferably 0.028 ⁇ m or more, further preferably 0.029 ⁇ m or more, particularly preferably 0.030 ⁇ m or more.
- the polypropylene resin composition for forming the surface layer (B) As a product, it is preferable to use a mixture of two or more polypropylene resins having different melt flow rates (MFR).
- MFR melt flow rates
- the MFR difference is preferably 3 g / 10 min or more, and more preferably 3.5 g / 10 min or more.
- the difference in the melt flow rate (MFR) of two or more kinds of polypropylene resins in the mixture of polypropylene resins is different, the crystallization speed and the degree of crystallization of each polypropylene are different. It is presumed that the arithmetic average roughness of the surface on the side opposite to the base material layer (A) of B) is 0.028 ⁇ m or more. Moreover, the arithmetic mean roughness of the surface of the surface layer (B) opposite to the base material layer (A) is unlikely to exceed 0.040 ⁇ m.
- the polypropylene resin having a smaller MFR a polymer obtained by copolymerizing propylene and ethylene and / or an ⁇ -olefin having 4 or more carbon atoms can also be used.
- the ⁇ -olefin having 4 or more carbon atoms include 1-butene, 1-hexene, 4-methyl / 1-pentene, 1-octene and the like.
- the total amount of ethylene and / or ⁇ -olefin having 4 or more carbon atoms and other copolymer components is preferably 8.0 mol% or less.
- the film When the copolymerization exceeds 8.0 mol%, the film may be whitened to have a poor appearance, or may become sticky and film formation may be difficult.
- These resins may be used in a blend of two or more. When blending, individual resins may be copolymerized in excess of 8.0 mol%, but the blend is preferably monomer units and monomers other than propylene at 8.0 mol% or less. .
- the polypropylene resin having a larger MFR a polymer obtained by copolymerizing the above propylene and ethylene and / or an ⁇ -olefin having 4 or more carbon atoms can be used, or a propylene homopolymer can be used. I can do it. It is preferable to use a propylene homopolymer.
- the polypropylene resin composition of the surface layer (B) of the biaxially oriented polypropylene film of the present invention preferably has an MFR of 1.0 g / 10 min to 8 g / 10 min.
- the lower limit of the MFR of the polypropylene resin composition of the surface layer (B) is more preferably 2 g / 10 minutes, and further preferably 3 g / 10 minutes.
- the upper limit of the MFR of the polypropylene resin composition of the surface layer (B) is more preferably 7 g / 10 minutes, and further preferably 6.0 g / 10 minutes. Within this range, the film-forming property is good and the appearance is also excellent.
- the MFR of the polypropylene resin composition of the surface layer (B) is smaller than 1.0 g / 10 min, the base layer (A) and the surface layer ( Since the viscosity difference of B) becomes large, unevenness (raw fabric unevenness) is likely to occur during film formation. If the MFR of the polypropylene resin composition of the surface layer (B) exceeds 8 g / 10 minutes, the adhesion to the cooling roll will be poor, air will be involved, the smoothness will be poor, and there will be many drawbacks starting from it. Therefore, it may be difficult to obtain an appropriate surface roughness.
- the surface specific resistance value of the surface of the surface layer (B) of the biaxially oriented polypropylene film of the present invention on the side opposite to the base material layer (A) is 15 Log ⁇ or more.
- the surface specific resistance value is more preferably 16 Log ⁇ or more.
- an additive of a low molecular weight compound such as an antistatic agent or an antifogging agent is not used as much as possible. If it is used, the additive contained in the base material layer (A) may bleed to the surface of the surface layer (B) on the opposite side of the base material layer (A).
- the surface specific resistance value 15 Log ⁇ or more it is preferable to perform physicochemical surface treatment such as corona treatment and flame treatment.
- physicochemical surface treatment such as corona treatment and flame treatment.
- the corona treatment it is preferable to discharge in the air using a preheating roll and a treatment roll.
- the wetting tension of the surface opposite to the base material layer (A) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is 38 mN / m or more.
- the wetting tension is 38 mN / m or more, the adhesiveness with the adhesive used for laminating with the printing ink or other member film is improved.
- additives such as antistatic agents and surfactants are usually used. However, these methods have an effect of reducing the surface resistivity. It is preferable to perform physicochemical surface treatment such as corona treatment and flame treatment.
- the corona treatment it is preferable to discharge in the air using a preheating roll and a treatment roll.
- the surface specific resistance value is mainly related to the strength of the corona treatment, but the wetting tension is also related to the bleed-out amount of the antistatic agent, so it is effective to set each in a suitable range.
- the surface layer (B) has a center surface peak height SR) on the side opposite to the base material layer (A) and a center surface valley depth SRv of 1.0 ⁇ m or more and 2.0 ⁇ m.
- SR center surface peak height
- SRv center surface valley depth
- the surface roughness of the surface layer (B) opposite to the base material layer (A) is the surface roughness center plane height SRp and the center plane valley depth SRv using a three-dimensional roughness meter.
- the center plane peak height SRp + center plane valley depth SRv of the surface opposite to the base layer (A) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is locally increased by an antiblocking agent or the like. It is an indicator of the state of the relatively large irregularities formed, for example, the biaxial orientation of the present invention having a surface layer (B) on at least one surface of the substrate layer (A) and the substrate layer (A) This is largely related to the slipperiness between the surface layer (B) and the base material layer (A) when the polypropylene film is rolled up.
- the surface layer (B) of the biaxially oriented polypropylene film of the present invention has a center surface peak height SRp + center surface valley depth SRv of the surface opposite to the base layer (A) of 1.0 ⁇ m or more, a roll The unwinding property from a film improves and transparency is maintained as it is 2.0 micrometers or less.
- the center plane peak height SRp + center plane valley depth SRv of the surface layer (B) opposite to the base material layer (A) is preferably 1.1 ⁇ m or more, more preferably 1.2 ⁇ m or more, and 1.3 ⁇ m or more. Is particularly preferred.
- the center plane peak height SRp + center plane valley depth SRv of the surface opposite to the base layer (A) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is 1.0 ⁇ m or more and 2.0 ⁇ m or less.
- an antiblocking agent is preferably added to the polypropylene resin composition forming the surface layer (B).
- the anti-blocking agent it can be appropriately selected from inorganic particles such as silica, calcium carbonate, kaolin and zeolite, and organic particles such as acrylic, polymethacrylic and polystyrene. . Among these, it is particularly preferable to use polymethacrylic particles.
- the average particle size of the antiblocking agent is preferably 1.0 to 2.5 ⁇ m, more preferably 1.0 to 2.0 ⁇ m.
- the measurement method of the average particle diameter here is a method in which a photograph is taken with a scanning electron microscope, the ferret diameter in the horizontal direction is measured using an image analyzer, and the average value is displayed.
- the antiblocking agent is preferably 0.15% by mass relative to the entire polypropylene resin or mixture thereof.
- the polypropylene resin used in the present invention is a polymer of propylene as a raw material alone or a copolymer of propylene and ethylene and / or ⁇ -olefin using a known catalyst such as a Ziegler-Natta catalyst or a metallocene catalyst. Is obtained. Among these, in order to eliminate the heterogeneous bond, it is preferable to use a Ziegler-Natta catalyst and a catalyst capable of polymerization with high stereoregularity.
- a known method may be employed, for example, a method of polymerizing in an inert solvent such as hexane, heptane, toluene, xylene, a method of polymerizing in a liquid monomer, or adding a catalyst to a gaseous monomer.
- an inert solvent such as hexane, heptane, toluene, xylene
- a method of polymerizing in a liquid monomer or adding a catalyst to a gaseous monomer.
- polymerizing combining these, etc. are mentioned.
- the base layer (A) of the biaxially oriented polypropylene film of the present invention of the present invention may contain additives and other resins.
- the additive include an antioxidant, an ultraviolet absorber, a nucleating agent, an adhesive, an antifogging agent, a flame retardant, and an inorganic or organic filler.
- the other resin include polypropylene resins other than the polypropylene resin used in the present invention, random copolymers that are copolymers of propylene and ethylene and / or ⁇ -olefins having 4 or more carbon atoms, and various elastomers.
- the base material layer (B) may contain additives and other resins.
- the additive include an antioxidant, an ultraviolet absorber, a nucleating agent, an adhesive, an antifogging agent, a flame retardant, and an inorganic or organic filler.
- the biaxially oriented polypropylene film of the present invention may be a film having a two-layer structure having a base layer (A) and a surface layer (B) one by one. It is good also as a structure more than a layer. Preferred is a two-layer structure of substrate layer (A) / surface layer (B), but surface layer (B) / A layer / surface layer (B), / substrate layer (A) / intermediate layer (C). ) / Surface layer (B) three-layer structure or more than that.
- the compositions may be different as long as each layer satisfies the characteristics.
- the total thickness of the biaxially oriented polypropylene film of the present invention is preferably 9 to 200 m, more preferably 10 to 150 ⁇ m, still more preferably 12 to 100 ⁇ m, and particularly preferably 12 to 80 ⁇ m.
- the thickness of the entire surface layer (B) / the thickness of the base material layer (A) is It is preferably from 0.01 to 0.5, more preferably from 0.02 to 0.4, and even more preferably from 0.03 to 0.3.
- the total thickness of the base layer (A) is preferably 50 to 99%, more preferably 60 to 97%, and particularly preferably 70 to 95% with respect to the total thickness of the film.
- the substantial thickness of the entire surface layer (B) is preferably 0.5 to 4 ⁇ m, more preferably 1 to 3.5 ⁇ m, and even more preferably 1.5 to 3 ⁇ m.
- the evaluation of the ink adhesion of the biaxially oriented polypropylene film of the present invention was carried out by performing a peel test of gravure-printed printing ink and performing the number of peeled portions out of the total 25 locations.
- the number of peeled portions is preferably 5 or less, more preferably 3 or less, and most preferably 0. If the number exceeds 5, the degree to which the printing ink peels becomes large, which is a problem. A method for evaluating ink adhesion will be described later.
- the lamination strength in the longitudinal direction after lamination to the biaxially oriented polypropylene film of the present invention is preferably 1.2 to 2.5 N / 15 mm, more preferably 1.3 to 2.5 N / mm, and 1.4 to 2.5 N / mm is more preferable. A method for measuring the laminate strength will be described later.
- the dynamic friction coefficient of the biaxially oriented polypropylene film of the present invention is preferably 0.5 or less, more preferably 0.48 or less, and particularly preferably 0.45 or less.
- the dynamic friction coefficient is 0.5 or less, the film can be smoothly unwound from the roll film, and printing is easy. A method for measuring the dynamic friction coefficient will be described later.
- the haze of the biaxially oriented polypropylene film of the present invention is preferably 5% or less, more preferably 0.2 to 5%, further preferably 0.3 to 4.5%, and particularly preferably 0.4 to 4%. . If it exceeds 5%, the transparency is inferior and the printed display may be difficult to see. For example, when the stretching temperature and heat setting temperature are too high, the haze tends to be worse when the cooling roll temperature is high, the cooling rate of the unstretched (raw material) sheet is slow, or when there are too many low molecular weight components. By doing so, it can be within the above range. A method for measuring haze will be described later.
- the biaxially oriented biaxially oriented polypropylene film of the present invention preferably has a heat shrinkage rate of 150% at 150 ° C. in the machine direction and the transverse direction, preferably 10% or less, more preferably 8% or less. It is particularly preferred. By setting the thermal shrinkage rate to 11% or less, it is possible to reduce the pitch deviation during printing. A method for measuring thermal shrinkage will be described later.
- the thermal shrinkage in the longitudinal direction at 150 ° C. is preferably 0.2 to 8%, more preferably 0.3 to 7%, and more preferably 0.5 to 6 % Is particularly preferred. If the heat shrinkage rate is in the above range, it can be said that the film has excellent heat resistance, and can be used in applications that may be exposed to high temperatures. If the thermal shrinkage at 150 ° C. is up to about 1.5%, for example, it is possible to increase the low molecular weight component, adjust the stretching conditions and the heat setting conditions, but in order to lower it below, anneal offline. It is preferable to perform the treatment.
- the tensile modulus in the machine direction of the biaxially oriented polypropylene film of the present invention is preferably 1.8 to 4 GPa, more preferably 2.1 to 3.7 GPa, and 2.2 to 3.5 GPa. Is more preferable, and 2.3 to 3.4 GPa is particularly preferable.
- the tensile modulus in the transverse direction is preferably 3.8 to 8 GPa, more preferably 4 to 7.5 GPa, still more preferably 4.1 to 7 GPa, and 4.2 to 6.5 GPa. Is particularly preferred. If the tensile elastic modulus is in the above range, the elasticity becomes strong and the film can be used even if the film thickness is small, so the amount of film used can be reduced. A method for measuring the tensile modulus will be described later.
- the lower limit of the plane orientation coefficient of the biaxially oriented polypropylene film of the present invention is preferably 0.011, more preferably 0.012, and even more preferably 0.013. Within the above range, the heat resistance and rigidity of the film tend to increase.
- the stretched laminated polypropylene film generally has a crystal orientation, and its direction and degree greatly affect the film properties. The degree of crystal orientation tends to change depending on the molecular structure of the polypropylene resin used and the process and conditions in film production, and can be adjusted to the above range by adjusting these. A method for measuring the plane orientation coefficient will be described later.
- the biaxially oriented polypropylene film of the present invention is obtained by melt-extruding the polypropylene resin composition for the base layer (A) and the polypropylene resin composition for the surface layer (B) by separate extruders. It is obtained by co-extrusion from a die, cooling with a cooling roll to form an unstretched sheet, stretching the unstretched sheet in the machine direction (MD) and the width direction (TD), and then heat setting. be able to.
- the melt extrusion temperature is preferably about 200 to 280 ° C.
- the polypropylene raw material for the base layer (A) and the polypropylene for the surface layer (B) The viscosity difference (MFR difference) of the raw materials is preferably 6 g / 10 minutes or less.
- MFR difference The viscosity difference
- the viscosity difference is larger than 6 g / 10 min, the layer is disturbed and the appearance is liable to be poor. More preferably, it is 5.5 g / 10 minutes or less, More preferably, it is 5 g / 10 minutes or less.
- the surface temperature of the cooling roll is preferably 25 to 35 ° C, more preferably 27 to 33 ° C. When the temperature exceeds 35 ° C., the film surface tends to be rough.
- the lower limit of the draw ratio in the machine direction (MD) is preferably 3 times, more preferably 3.5 times. If it is less than the above, film thickness unevenness may occur.
- the upper limit of the MD draw ratio is preferably 8 times, more preferably 7 times. When the above is exceeded, it may be difficult to carry out TD stretching continuously.
- the lower limit of the MD stretching temperature is preferably 120 ° C, more preferably 125 ° C, and even more preferably 130 ° C. If it is less than the above, the mechanical load may increase, the thickness unevenness may increase, or the film surface may be roughened.
- the upper limit of the MD stretching temperature is preferably 150 ° C, more preferably 145 ° C, and further preferably 140 ° C. A higher temperature is preferable for lowering the thermal shrinkage, but it may adhere to the roll and cannot be stretched, or surface roughness may occur.
- the lower limit of the draw ratio in the width direction (TD) is preferably 4 times, more preferably 5 times, and even more preferably 6 times. If it is less than the above, thickness unevenness may occur.
- the upper limit of the TD stretch ratio is preferably 20 times, more preferably 17 times, still more preferably 15 times, and particularly preferably 12 times. If the above is exceeded, the thermal shrinkage rate may be increased or the film may be broken during stretching.
- the preheating temperature in TD stretching is preferably set to 5 to 15 ° C. higher than the stretching temperature in order to quickly raise the film temperature in the vicinity of the stretching temperature. The TD stretching is performed at a higher temperature than the conventional stretched polypropylene film.
- the lower limit of the TD stretching temperature is preferably 155 ° C, more preferably 157 ° C, still more preferably 158 ° C, and particularly preferably 160 ° C. If it is less than the above, it may break without being sufficiently softened, or the thermal shrinkage rate may be increased.
- the upper limit of the TD stretching temperature is preferably 170 ° C, more preferably 168 ° C, and further preferably 163 ° C. In order to lower the thermal shrinkage rate, it is preferable that the temperature is higher. However, if the temperature is higher than the above, the low molecular component is melted and recrystallized to lower the orientation, and the surface may be roughened or the film may be whitened.
- the stretched film is heat-set.
- the heat setting can be performed at a higher temperature than a conventional stretched polypropylene film.
- the lower limit of the heat setting temperature is preferably 165 ° C, more preferably 166 ° C. If it is less than the above, the thermal shrinkage rate may increase. In addition, a long time treatment is required to lower the heat shrinkage rate, and productivity may be inferior.
- the upper limit of the heat setting temperature is preferably 176 ° C, more preferably 175 ° C. When the above is exceeded, the low molecular component may melt and recrystallize, and the surface roughness or the film may be whitened.
- the lower limit of relaxation (relaxation) is preferably 2%, more preferably 3%. If it is less than the above, the thermal shrinkage rate may increase.
- the upper limit of relaxation (relaxation) is preferably 10%, more preferably 8%. When the above is exceeded, the thickness unevenness may increase.
- the film produced in the above process can be once wound into a roll and then annealed offline.
- the lower limit of the offline annealing temperature is preferably 160 ° C, more preferably 162 ° C, and even more preferably 163 ° C. If it is less than the above, the effect of annealing may not be obtained.
- the upper limit of the offline annealing temperature is preferably 175 ° C., more preferably 174 ° C., and further preferably 173 ° C. When the above is exceeded, the transparency may decrease, or the thickness unevenness may increase.
- the lower limit of the offline annealing time is preferably 0.1 minutes, more preferably 0.5 minutes, and even more preferably 1 minute. If it is less than the above, the effect of annealing may not be obtained.
- the upper limit of the offline annealing time is preferably 30 minutes, more preferably 25 minutes, and further preferably 20 minutes. When the above is exceeded, productivity may be reduced.
- the biaxially oriented polypropylene film thus obtained can be subjected to corona discharge, plasma treatment, flame treatment, etc., if necessary, and then wound with a winder to obtain the biaxially oriented polypropylene film roll of the present invention. it can.
- the biaxially oriented polypropylene film of the present invention can be widely used, for example, for applications in which processing such as printing ink or lamination is performed.
- the measuring method of the film physical property obtained by the Example and the comparative example is as follows.
- the mesopentad fraction ([mmmm]%) was measured using 13C-NMR.
- the mesopentad fraction was calculated according to the method described in “Zambelli et al., Macromolecules, Vol. 6, 925 (1973)”.
- the 13C-NMR measurement was performed at 110 ° C. by using “AVANCE 500” manufactured by BRUKER, and dissolving 200 mg of a sample in an 8: 2 (volume ratio) mixture of o-dichlorobenzene and heavy benzene at 135 ° C.
- Melt flow rate (MFR; g / 10 min) According to JIS K7210, the temperature was 230 ° C. and the load was 2.16 kgf. In the case of a raw material resin, pellets (powder) were used as they were by weighing out the required amount. In the case of a film, after cutting out a necessary amount, a sample cut into about 5 mm square was used.
- the number average molecular weight (Mn), the mass average molecular weight (Mw), and the molecular weight distribution are respectively represented by the molecular number (N i ) of the molecular weight (M i ) at each elution position of the GPC curve obtained through the molecular weight calibration curve. It is defined by an expression.
- each of the base layer (A) and the surface layer (B) is measured by cutting a cross section of a biaxially stretched laminated polypropylene film hardened with a modified urethane resin with a microtome and observing with a differential interference microscope. did.
- Thermal shrinkage (%) Based on JIS Z1712, it measured by the following method. The film was cut into a width of 20 mm and a length of 200 mm in each of the MD direction and the TD direction, suspended in a hot air oven at 150 ° C. and heated for 5 minutes. The length before and after heating was measured, the ratio (%) of the length obtained by subtracting the length after heating from the length before heating to the length before heating was determined, and the thermal shrinkage rate was determined.
- Refractive index, plane orientation coefficient Measured using an Atago Abbe refractometer according to JIS K7142-1996 5.1 (Method A).
- the refractive indexes along the MD and TD directions were Nx and Ny, respectively, and the refractive index in the thickness direction was Nz.
- the plane orientation coefficient ( ⁇ P) was determined by (Nx + Ny) / 2 ⁇ Nz.
- the surface roughness of the obtained film was evaluated using a three-dimensional roughness meter (manufactured by Kosaka Laboratories, model number ET-30HK) at a stylus pressure of 20 mg and measured length in the X direction. 1 mm, feed speed 100 ⁇ m / second, Y-direction feed pitch 2 ⁇ m, 99 recording lines, height direction magnification 20000 times, cut-off 80 ⁇ m were measured, and the arithmetic average roughness described in JISB 0601 (1994) was measured. Calculated according to the definition. Arithmetic average roughness (SRa), center plane mountain height (SRp), and center plane valley depth (SRv) were each evaluated three times and evaluated by their average values.
- SRa center plane mountain height
- SRv center plane valley depth
- the wet tension is determined by observing the liquid film of the test liquid mixture in a bright place and in the liquid film state after 3 seconds. It is wet to maintain the state when applied for 3 seconds or more without causing the liquid film to break. When the wetting is maintained for 3 seconds or more, the process proceeds to a liquid mixture having the next highest surface tension. Conversely, when the liquid film is broken within 3 seconds or less, the process proceeds to the next liquid mixture having a low surface tension. This operation is repeated, and a liquid mixture that can accurately wet the surface of the test piece in 3 seconds is selected.
- Step 3) Use a new swab for each test. The brush or wire bar is washed with methanol and dried after each use because the remaining liquid changes its composition and surface tension by evaporation.
- Step 4) The operation of selecting a mixed solution that can wet the surface of the test piece in 3 seconds is performed at least three times. The surface tension of the mixture thus selected is reported as the wetting tension of the film.
- Cross-section peeling part 0 ⁇ : Excellent in printing ink adhesion. ⁇ 1 to 5 ... ⁇ : Good adhesion of printing ink. 6 6 to 15 ⁇ ⁇ ⁇ ⁇ : Poor adhesion to printing ink. ⁇ 1 or more ⁇ ⁇ : No printing ink adhesion.
- Laminate strength The laminate strength was measured by the following procedure.
- Procedure 1) Preparation of a laminate film with a sealant film A continuous dry laminating machine was used as follows.
- the surface layer (B) surface of the biaxially oriented polypropylene film obtained in Examples and Comparative Examples was gravure-coated so that the coating amount when dried was 3.0 g / m 2, and then led to the drying zone. Dried at 80 ° C. for 5 seconds. Subsequently, it was bonded to a sealant film between rolls provided on the downstream side (roll pressure 0.2 MP, roll temperature: 60 ° C.).
- the obtained laminate film was subjected to an aging treatment at 40 ° C. for 3 days while being wound up.
- the adhesive was obtained by mixing 17.9% by mass of a main agent (manufactured by Toyo Morton, TM329), 17.9% by mass of a curing agent (CAT8B, manufactured by Toyo Morton) and 64.2% by mass of ethyl acetate.
- An ether adhesive was used, and a non-stretched polypropylene film (Pyrene (registered trademark) CTP1128, thickness 30 ⁇ m) manufactured by Toyobo Co., Ltd. was used as the sealant film.
- Procedure 2 Measurement of laminate strength
- the laminate film obtained above was cut into a strip shape (length: 200 mm, width: 15 mm) having a long side in the longitudinal direction of a biaxially oriented polypropylene film, and a tensile tester (Tensilon, Orientec) Was used, and the peel strength (N / 15 mm) at the time of T-peeling at a tensile rate of 200 mm / min in an environment of 23 ° C. was measured. The measurement was performed three times, and the average value was taken as the laminate strength.
- Example 1 Polypropylene homopolymer PP-1 shown in Table 1 was used for the base material layer (A).
- the surface layer (B) 49% by weight of the polypropylene homopolymer PP-1 shown in Table 1 and 51 parts by weight of the ethylene copolymer polypropylene polymer PP-3 shown in Table 1 were mixed. What mixed the quantity corresponding to 0.15 mass% of the said mixture was used for the thing by using commercially available polymethylmethacrylate (PMMA) particle
- PMMA polymethylmethacrylate
- the melt flow rate (g / 10 min) of a mixture of 49% by weight of the polypropylene homopolymer PP-1 and 51% by weight of the ethylene copolymer polypropylene polymer PP-3 was 5.3.
- the base material layer (A) was melted at 250 ° C. using a 60 mm extruder and the surface layer (B) was a 65 mm extruder, respectively, and coextruded into two layers in a sheet form from a T die. After the (A) side was in contact with the cooling roll and cooled and solidified with a 30 ° C. cooling roll, it was stretched 4.5 times in the longitudinal direction (MD) of 125 ° C.
- the film width direction both ends are clipped, preheated at 170 ° C., stretched 8.2 times in the width direction (TD) at 158 ° C., and relaxed by 6.7% in the width direction (TD). And heat-fixed at 165 ° C.
- the film forming condition at this time was defined as film forming condition a.
- the corona treatment was performed on the surface layer (B) side of the biaxially oriented polypropylene film using a corona treatment machine manufactured by Sophtal Corona & Plasma GmbH under the condition of applied current value: 0.75A, I wound it up with a winder.
- the thickness of the obtained film was 20 ⁇ m.
- Example 2 The resin used for the base material layer (A) is changed to polypropylene resin PP-2, the base material layer (A) is a 60 mm extruder and the surface layer (B) is a 65 mm extruder, and the raw material resin is 250 ° C. respectively. And then coextruded into a sheet form from a T-die, cooled and solidified with a 30 ° C. cooling roll, and then stretched 4.5 times in the 135 ° C. longitudinal direction (MD). Next, in the tenter, both ends in the film width direction are sandwiched between clips, preheated at 175 ° C., stretched 8.2 times in the width direction (TD) at 160 ° C., and relaxed by 6.7% in the width direction (TD).
- TD width direction
- Example 3 A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that the thickness of the base material layer (A) was changed to 38 ⁇ m.
- Example 4 A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that the thickness of the base material layer (A) was changed to 18 ⁇ m.
- Example 2 A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that polypropylene homopolymers PP-1 and PP-4 were used for the surface layer (B).
- Example 5 A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that the surface layer (B) side of the biaxially oriented polypropylene film was not subjected to corona treatment.
- Table 2 Table 3, and Table 4 show the raw materials used in the above Examples and Comparative Examples, the film forming conditions, and the physical properties of the obtained films, respectively.
- the biaxially stretched laminated polypropylene films obtained in Examples 1 to 4 had high laminate strength and excellent printing ink adhesion. Furthermore, the thermal shrinkage rate was low and the Young's modulus was high. On the other hand, the films of Comparative Examples 1 to 5 were all poor in printing ink adhesion. Moreover, all the films of Comparative Example 6 had high haze and were inferior in transparency.
- the biaxially stretched laminated polypropylene film of the present invention has good printing ink adhesion, it can be used not only for food packaging used for confectionery, but also for labels, etc. Since it can be manufactured, it is industrially useful.
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Abstract
Description
本発明は、二軸配向ポリプロピレン系フィルムに関する。詳細には、印刷インキとの密着性や他部材フィルムとのラミネートに使用する接着剤との密着性に優れる二軸延伸ポリプロピレン系フィルムに関する。 The present invention relates to a biaxially oriented polypropylene film. Specifically, the present invention relates to a biaxially stretched polypropylene film having excellent adhesion to printing ink and adhesion to an adhesive used for laminating with other member films.
従来、二軸配向ポリプロピレン系フィルムは、その透明性や機械的特性において非常に優れたものであるところから、食品や繊維製品などを始めとする様々の物品の包装材料として広く用いられている。しかしながら、ポリプロピレン系フィルムの問題点としては、例えば、ポリプロピレン系樹脂が無極性であることから表面エネルギーが小さく、そのために印刷インキやラミネート等の加工において印刷インキあるいは他素材との接着性が十分ではないことが指摘されている。 Conventionally, biaxially oriented polypropylene-based films are widely used as packaging materials for various articles such as foods and textile products because of their excellent transparency and mechanical properties. However, as a problem of polypropylene film, for example, since polypropylene resin is nonpolar, the surface energy is small, and therefore, the adhesiveness with printing ink or other materials is not sufficient in processing of printing ink or laminate, etc. It has been pointed out that there is no.
特に、二軸配向ポリプロピレン系フィルムを包装材料として使用する場合には、接着剤を用いて、他部材フィルムとのラミネートが施されることが一般に行われるが、これらのフィルム同士のラミネート強度が弱い場合には、包装材料としての強度が弱くなり破れて内容物がはみ出したり、また、袋の破れた部分を通して酸素や水蒸気が出入りし、食品包材としての役目を果たさなかったりすることが問題点として挙げられる。 In particular, when a biaxially oriented polypropylene film is used as a packaging material, it is generally performed to laminate with another member film using an adhesive, but the laminate strength between these films is weak. In some cases, the strength of the packaging material is weakened and it breaks and the contents protrude, and oxygen and water vapor enter and exit through the torn part of the bag, so that it does not serve as a food packaging material. As mentioned.
また、二軸配向ポリプロピレン系フィルムは印刷を施されることも一般的であるが、その印刷の発色性、色落ちの観点から、インキの印刷ロールから二軸配向ポリプロピレン系フィルムの表面への印刷インキの転移性や印刷インキのフィルム表面への密着性の向上がより求められている。 In addition, biaxially oriented polypropylene film is generally printed, but from the viewpoint of color development and color fading, printing from the ink printing roll to the surface of the biaxially oriented polypropylene film. Improvements in ink transferability and adhesion of printing ink to the film surface are more demanded.
このような問題点に対する対策として様々の方法が提案されており、例えば、プロピレン-エチレンランダム共重合体に有機ポリマー微粒子を配合した組成物からなるスキン層を二軸配向ポリプリロピレンフィルムの表面に積層したフィルムが開示されている(例えば、特許文献1等参照。)が、印刷インキの密着性が不十分であるばかりか、スキン層を別途設ける工程を必要とし、生産性に劣る。 Various methods have been proposed as countermeasures against such problems. For example, a skin layer composed of a composition in which organic polymer fine particles are blended with a propylene-ethylene random copolymer is formed on the surface of a biaxially oriented polypropylene film. Although a laminated film is disclosed (for example, see Patent Document 1), not only the adhesion of the printing ink is insufficient, but also a process of separately providing a skin layer is required, resulting in poor productivity.
本発明は、二軸配向ポリプロピレン系フィルムが本来有している優れた透明性や機械的特性を損なうことなく、他部材フィルムとのラミネート強度が大きく、また、印刷ロールからフィルムへの印刷インキ転移性や印刷インキの密着性に優れた、二軸配向ポリプリロピレンフィルムを提供することを目的とする。 The present invention does not impair the excellent transparency and mechanical properties inherent in the biaxially oriented polypropylene film, has a high lamination strength with other member films, and transfers printing ink from the printing roll to the film. It is an object to provide a biaxially oriented polypropylene film having excellent properties and adhesion of printing ink.
上記課題を解決し得た本発明は、ポリプロピレン系樹脂を主成分とする基材層(A)と基材層(A)の少なくとも一方の表面にポリプロピレン系樹脂を主成分とする表面層(B)とを有し、表面層(B)の基材層(A)とは反対側の表面の表面粗さが0.027μm以上、0.040μm以下であり、表面層(B)の基材層(A)とは反対側の表面の表面固有抵抗値が15LogΩ以上であり、表面層(B)の基材層(A)とは反対側の表面の濡れ張力が38mN/m以上であり、フィルム厚みが20μm以上、50μm以下であり、及びフィルムのヘーズ(透明)値が5%以下であることを特徴とする二軸配向ポリプロピレン系フィルムである。 The present invention that has solved the above problems is a surface layer (B) having a polypropylene resin as a main component on at least one surface of a base material layer (A) having a polypropylene resin as a main component and a substrate layer (A). The surface roughness of the surface of the surface layer (B) opposite to the substrate layer (A) is 0.027 μm or more and 0.040 μm or less, and the substrate layer of the surface layer (B) The surface resistivity of the surface opposite to (A) is 15 LogΩ or more, the wetting tension of the surface of the surface layer (B) opposite to the base material layer (A) is 38 mN / m or more, and the film The biaxially oriented polypropylene film is characterized in that the thickness is 20 μm or more and 50 μm or less, and the haze (transparency) value of the film is 5% or less.
前記表面層(B)の基材層(A)とは反対側の表面の中心面山高さSRp+中心面谷深さが1.0μm以上2.0μm以下であるのが好適である。 It is preferable that the center surface peak height SRp + center surface valley depth of the surface of the surface layer (B) opposite to the base material layer (A) is 1.0 μm or more and 2.0 μm or less.
前記二軸配向ポリプロピレン系フィルムの縦方向および横方向の150℃での熱収縮率が11%以下であるのが好適である。 It is preferable that the heat shrinkage rate at 150 ° C. in the longitudinal direction and the transverse direction of the biaxially oriented polypropylene film is 11% or less.
前記のいずれかに記載の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層と反対側に印刷層を有する積層体が好適である。 A laminate having a printing layer on the side opposite to the substrate layer of the surface layer (B) of the biaxially oriented polypropylene film described in any one of the above is preferable.
本発明の二軸配向ポリプロピレン系フィルムは、二軸配向ポリプロピレン系フィルムが本来有している優れた透明性や機械的特性を損なうことなく、他部材フィルムとのラミネート強度が大きく、また、印刷ロールからフィルムへの印刷インキ転移性や印刷インキの密着性に優れ、また効率よく生産できるようになった。 The biaxially oriented polypropylene film of the present invention has a large laminate strength with other member films without impairing the excellent transparency and mechanical properties inherent to the biaxially oriented polypropylene film, and a printing roll The film is excellent in transferability of printing ink from film to film and adhesion of printing ink, and can be produced efficiently.
本発明の二軸配向ポリプロピレン系フィルムは、ポリプロピレン系樹脂を主成分とする基材層(A)と基材層(A)の少なくとも一方の表面にポリプロピレン系樹脂を主成分とする表面層(B)とを有し、表面層(B)の基材層(A)とは反対側の表面の算術平均粗さが0.027μm以上、0.040μm以下であり、表面層(B)の基材層(A)とは反対側の表面の表面固有抵抗値が15LogΩ以上であり、表面層(B)の基材層(A)とは反対側の表面の濡れ張力が38mN/m以上であり、フィルム厚みが20μm以上、50μm以下であり、及びフィルムのヘーズ値が5%以下であることを特徴とする。
ここで、表面層(B)の基材層(A)とは反対側の表面の算術表面粗さSRaとは、三次元粗さ計を使用し、触針圧20mgにて、X方向の測定長さ1mm、Y方向の送りピッチ2μmで収録ライン数99本、高さ方向倍率20000倍、カットオフ80μmの測定を行い、JISB 0601(1994)に記載の算術平均粗さの定義に準じて、のである。
The biaxially oriented polypropylene film of the present invention has a surface layer (B) containing a polypropylene resin as a main component on at least one surface of a base material layer (A) and a base material layer (A) containing a polypropylene resin as a main component. The arithmetic average roughness of the surface of the surface layer (B) opposite to the substrate layer (A) is 0.027 μm or more and 0.040 μm or less, and the substrate of the surface layer (B) The surface resistivity of the surface opposite to the layer (A) is 15 LogΩ or more, and the wetting tension of the surface of the surface layer (B) opposite to the base material layer (A) is 38 mN / m or more, The film thickness is 20 μm or more and 50 μm or less, and the haze value of the film is 5% or less.
Here, the arithmetic surface roughness SRa of the surface layer (B) opposite to the base material layer (A) is measured in the X direction using a three-dimensional roughness meter at a stylus pressure of 20 mg. The length of 1 mm, the feed pitch in the Y direction is 2 μm, the number of recorded lines is 99, the height direction magnification is 20000 times, and the cutoff is 80 μm. According to the definition of arithmetic mean roughness described in JISB 0601 (1994), It is.
算術平均粗さSRaは1つの突出して大きな山や谷の影響を受けにくく、アンチブロッキング剤や滑剤により局所的に形成された比較的大きな山や谷の部分以外の表面に形成される比較的小さな凹凸状のうねりを表わす指標となる。印刷インキの大部分はアンチブロッキング剤や滑剤により形成された比較的大きな山や谷の部分以外の表面に付着するため、印刷インキの密着性と大きな関係がある。これは、後述する中心面山高さSRpと中心面谷深さSRvとは異なる。
また、表面層(B)の基材層(A)とは反対側の表面の表面固有抵抗値は、表面に存在する帯電防止剤の量を羽異するものであり、表面に存在する帯電防止剤の量が少ないほど表面抵抗値は大きくなる。
さらに、表面層(B)の濡れ張力は、フィルム表面をぬらすと判定された混合液試薬の表面張力(μN/cm)の数値を表わし、印刷インキや接着剤の濡れやすさと関係するものである。
さらに下記で詳細に説明する。
Arithmetic average roughness SRa is not easily affected by one protruding large peak or valley, and is relatively small formed on a surface other than a relatively large peak or valley formed locally by an antiblocking agent or lubricant. It becomes an index that represents uneven undulations. Since most of the printing ink adheres to the surface other than the relatively large peaks and valleys formed by the antiblocking agent or lubricant, it has a great relationship with the adhesion of the printing ink. This is different from the center plane mountain height SRp and the center plane valley depth SRv described later.
Further, the surface specific resistance value of the surface layer (B) opposite to the base material layer (A) is different from the amount of the antistatic agent present on the surface, and the antistatic material existing on the surface. The surface resistance value increases as the amount of the agent decreases.
Further, the wetting tension of the surface layer (B) represents the numerical value of the surface tension (μN / cm) of the mixed solution reagent determined to wet the film surface, and is related to the wettability of the printing ink and the adhesive. .
Further details will be described below.
(1)基材層(A)
本発明の二軸配向ポリプロピレン系フィルムの基材層(A)に用いるポリプロピレン系樹脂は、プロピレンの重合体もしくは、プロピレンとエチレンおよび/または炭素数4以上のα-オレフィンを0.5モル%以下で共重合した重合体をいう。共重合体における共重合成分は0.3モル%以下が好ましく、0.1モル%以下がより好ましく、共重合成分を含まない完全ホモポリプロピレンが最も好ましい。
エチレンおよび/または炭素数4以上のα-オレフィンは、0.5モル%を超えて共重合すると、結晶性や剛性が低下し過ぎて、高温での熱収縮率が大きくなることがある。この様な樹脂をブレンドして用いても良い。
(1) Base material layer (A)
The polypropylene resin used for the base layer (A) of the biaxially oriented polypropylene film of the present invention is a propylene polymer or propylene and ethylene and / or an α-olefin having 4 or more carbon atoms of 0.5 mol% or less. Refers to a polymer copolymerized with The copolymer component in the copolymer is preferably 0.3 mol% or less, more preferably 0.1 mol% or less, and most preferably complete homopolypropylene containing no copolymer component.
When ethylene and / or an α-olefin having 4 or more carbon atoms is copolymerized in excess of 0.5 mol%, the crystallinity and rigidity may be excessively lowered, and the thermal shrinkage at high temperatures may increase. You may blend and use such resin.
本発明の二軸配向ポリプロピレン系フィルムの基材層(A)を構成するポリプロピレン系樹脂の立体規則性の指標である13C-NMRで測定されるメソペンタッド分率([mmmm]%)は、98~99.5%であることが好ましい。より好ましくは、98.1%以上であり、さらに好ましくは98.2%以上である。ポリプロピレン系樹脂のメソペンタッド率が小さいと、弾性率が低くなり、耐熱性が不充分となるおそれがある。99.5%が現実的な上限である。 The mesopentad fraction ([mmmm]%) measured by 13C-NMR, which is an index of stereoregularity of the polypropylene resin constituting the base material layer (A) of the biaxially oriented polypropylene film of the present invention, is 98 to It is preferable that it is 99.5%. More preferably, it is 98.1% or more, More preferably, it is 98.2% or more. When the mesopentad ratio of the polypropylene resin is small, the elastic modulus is low and the heat resistance may be insufficient. 99.5% is a realistic upper limit.
本発明の二軸配向ポリプロピレン系フィルムの基材層(A)を構成するポリプロピレン系樹脂の質量平均分子量(Mw)は、180,000~500,000が好ましい。
180,000より小さいと、溶融粘度が低いため、キャスト時に安定せず、製膜性が悪くなることがある。Mwが500,000を超えると、分子量10万以下の成分の量が35質量%となり、高温での熱収縮率が低減する。
より好ましいMwの下限は190,000、さらに好ましくは200,000であり、より好ましいMwの上限は320,000、さらに好ましくは300,000、特に好ましくは250,000である。
The mass average molecular weight (Mw) of the polypropylene resin constituting the substrate layer (A) of the biaxially oriented polypropylene film of the present invention is preferably 180,000 to 500,000.
If it is less than 180,000, the melt viscosity is low, so that it is not stable at the time of casting, and the film-forming property may deteriorate. When Mw exceeds 500,000, the amount of the component having a molecular weight of 100,000 or less becomes 35% by mass, and the heat shrinkage rate at high temperature is reduced.
The lower limit of Mw is more preferably 190,000, still more preferably 200,000, and the upper limit of more preferable Mw is 320,000, more preferably 300,000, particularly preferably 250,000.
本発明の二軸配向ポリプロピレン系フィルムの基材層(A)を構成するポリプロピレン系樹脂の数平均分子量(Mn)は、20,000~200,000が好ましい。
20,000より小さいと、溶融粘度が低いため、キャスト時に安定せず、製膜性が悪くなることがある。200,000を超えると、高温での熱収縮率が低減する。
より好ましいMnの下限は30,000、さらに好ましくは40,000、特に好ましくは50,000であり、より好ましいMnの上限は80,000、さらに好ましくは70,000、特に好ましくは60,000である。
また、上記ポリプロピレンに高分子量成分を加えると、高分子量成分が低分子量成分の結晶化を促進する面があるが、分子同士の絡み合いが強くなり、結晶性が高くても熱収縮率が大きくなる傾向もある。ある。Mw/Mnが大きくなりすぎると高分子量成分が多くなり熱収縮率が大きくなる場合があり好ましくない。高分子量成分を加えても、Mw/Mnを5.5~20以下の範囲とするのが良い。
The number average molecular weight (Mn) of the polypropylene resin constituting the base layer (A) of the biaxially oriented polypropylene film of the present invention is preferably 20,000 to 200,000.
If it is less than 20,000, the melt viscosity is low, so that it is not stable at the time of casting, and the film-forming property may deteriorate. When it exceeds 200,000, the thermal shrinkage rate at a high temperature is reduced.
The lower limit of Mn is more preferably 30,000, more preferably 40,000, particularly preferably 50,000, and the upper limit of Mn is more preferably 80,000, still more preferably 70,000, particularly preferably 60,000. is there.
In addition, when a high molecular weight component is added to the polypropylene, the high molecular weight component promotes crystallization of a low molecular weight component, but the entanglement between molecules becomes strong, and the thermal shrinkage rate increases even if the crystallinity is high. There is also a trend. is there. If Mw / Mn is too large, the high molecular weight component increases and the thermal shrinkage rate may increase, which is not preferable. Even if a high molecular weight component is added, Mw / Mn is preferably in the range of 5.5 to 20 or less.
また、分子量分布の指標であるMw/Mnは、基材層(A)のポリプロピレン系樹脂では2.8~8が好ましい。より好ましくは2.8~7、さらに好ましくは2.8~6であり、特に好ましくは2.8~5.4である。また、下限は3以上が好ましく、3.3以上がより好ましい。
なお、ポリプロピレン系樹脂の分子量分布は、異なる分子量の成分を多段階に一連のプラントで重合したり、異なる分子量の成分をオフラインで混錬機でブレンドしたり、異なる性能をもつ触媒をブレンドして重合したり、所望の分子量分布を実現できる触媒を用いたりすることで調整することが可能である。
In addition, Mw / Mn, which is an index of molecular weight distribution, is preferably 2.8 to 8 in the polypropylene resin of the base material layer (A). More preferably, it is 2.8 to 7, more preferably 2.8 to 6, and particularly preferably 2.8 to 5.4. Further, the lower limit is preferably 3 or more, and more preferably 3.3 or more.
The molecular weight distribution of polypropylene resin is determined by polymerizing different molecular weight components in a series of plants in multiple stages, blending different molecular weight components offline in a kneader, or blending catalysts with different performance. It can be adjusted by polymerizing or using a catalyst capable of realizing a desired molecular weight distribution.
本発明の二軸配向ポリプロピレン系フィルムの基材層(A)のポリプロピレン系樹脂は、Mw/Mnが2.8~5.4の範囲の場合は、メルトフローレート(MFR;230℃、2.16kgf)が4g/10分~20g/10分であることが好ましい。
基材層(A)のポリプロピレン系樹脂のMFRの下限は、5g/10分であることがより好ましく、6g/10分であることがさらに好ましく、7g/10分であることが特に好ましい。基材層(A)のポリプロピレン系樹脂のMFRの上限は、15g/10分であることがより好ましく、12g/10分であることがさらに好ましい。
基材層(A)のポリプロピレン系樹脂のMw/Mn及びMFRが、この範囲であると、高温での熱収縮率も小さく保つことができる、また、冷却ロールへの密着性も良好で製膜性に優れる。
When the Mw / Mn is in the range of 2.8 to 5.4, the polypropylene resin of the base layer (A) of the biaxially oriented polypropylene film of the present invention has a melt flow rate (MFR: 230 ° C., 2. 16 kgf) is preferably from 4 g / 10 min to 20 g / 10 min.
The lower limit of the MFR of the polypropylene resin of the base material layer (A) is more preferably 5 g / 10 minutes, further preferably 6 g / 10 minutes, and particularly preferably 7 g / 10 minutes. The upper limit of the MFR of the polypropylene resin of the base material layer (A) is more preferably 15 g / 10 minutes, and further preferably 12 g / 10 minutes.
When the Mw / Mn and MFR of the polypropylene resin of the base material layer (A) are within this range, the heat shrinkage rate at high temperatures can be kept small, and the film has good adhesion to the cooling roll. Excellent in properties.
(2)表面層(B)
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の表面粗さが0.027μm以上、0.040μm以下であることが好適である。0.027μm未満であると、印刷インキとの密着性や他部材フィルムとのラミネート強度が十分でなく、0.040μm以上を越えると、ヘイズが大きくなったり、印刷の発色性が悪くなるという問題が生じる。
表面層(B)の基材層(A)とは反対側の表面の表面粗さは0.028μm以上がより好ましく、0.029μm以上がさらに好ましく、0.030μm以上が特に好ましい。
表面層(B)の基材層(A)とは反対側の表面の表面粗さが0.027μm以上、0.040μm以下とするためには、表面層(B)を形成するポリプロピレン系樹脂組成物として、メルトフローレート(MFR)が異なる2種以上のポリプロピレン系樹脂の混合物を使用することが好ましい。この場合、のMFRの差は3g/10分以上であることが好ましく、3.5g/10分以上であることがより好ましい。
上記のように、ポリプロピレン系樹脂の混合物中の2種以上のポリプロピレン系樹脂のメルトフローレート(MFR)の差が異なると、それぞれのポリプリピレンの結晶化速度や結晶化度が異なるため、表面層(B)の基材層(A)とは反対側の表面の算術平均粗さが0.028μm以上となるものと推測している。また、表面層(B)の基材層(A)とは反対側の表面の算術平均粗さは0.040μmを超えにくくなる。
MFRが小さい方のポリプロピレン系樹脂としては、プロピレンとエチレンおよび/または炭素数4以上のα-オレフィンを共重合した重合体も用いることができる。炭素数4以上のα-オレフィンとしては、1-ブテン、1-ヘキセン、4-メチル・1-ペンテン、1-オクテンなどが挙げられる。また、その他の共重合成分として極性を有するマレイン酸等を使用しても良い。
エチレンおよび/または炭素数4以上のα-オレフィン、その他の共重合成分は合計で8.0モル%以下であることが好ましい。8.0モル%を超えて共重合すると、フィルムが白化して外観不良となったり、粘着性が生じて製膜が困難となったりする場合がある。
また、これらの樹脂は2種以上をブレンドして用いても良い。ブレンドする場合、個々の樹脂は8.0モル%を超えて共重合されたものであっても良いが、ブレンド物はモノマー単位でプロピレン以外のモノマーは8.0モル%以下であることが好ましい。
また、MFRが大きい方のポリプロピレン系樹脂としては、上記プロピレンとエチレンおよび/または炭素数4以上のα-オレフィンを共重合した重合体を用いることも出来るし、プロピレン単独重合体を使用することも出来る。プロピレン単独重合体を使用することが好ましい。
(2) Surface layer (B)
It is preferable that the surface roughness of the surface layer (B) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is 0.027 μm or more and 0.040 μm or less. If it is less than 0.027 μm, the adhesion to the printing ink and the laminate strength with other member films are not sufficient, and if it exceeds 0.040 μm, the haze increases or the color developability of printing deteriorates. Occurs.
The surface roughness of the surface layer (B) opposite to the base material layer (A) is more preferably 0.028 μm or more, further preferably 0.029 μm or more, particularly preferably 0.030 μm or more.
In order for the surface roughness of the surface of the surface layer (B) opposite to the base material layer (A) to be 0.027 μm or more and 0.040 μm or less, the polypropylene resin composition for forming the surface layer (B) As a product, it is preferable to use a mixture of two or more polypropylene resins having different melt flow rates (MFR). In this case, the MFR difference is preferably 3 g / 10 min or more, and more preferably 3.5 g / 10 min or more.
As described above, if the difference in the melt flow rate (MFR) of two or more kinds of polypropylene resins in the mixture of polypropylene resins is different, the crystallization speed and the degree of crystallization of each polypropylene are different. It is presumed that the arithmetic average roughness of the surface on the side opposite to the base material layer (A) of B) is 0.028 μm or more. Moreover, the arithmetic mean roughness of the surface of the surface layer (B) opposite to the base material layer (A) is unlikely to exceed 0.040 μm.
As the polypropylene resin having a smaller MFR, a polymer obtained by copolymerizing propylene and ethylene and / or an α-olefin having 4 or more carbon atoms can also be used. Examples of the α-olefin having 4 or more carbon atoms include 1-butene, 1-hexene, 4-methyl / 1-pentene, 1-octene and the like. Moreover, you may use the maleic acid etc. which have polarity as another copolymerization component.
The total amount of ethylene and / or α-olefin having 4 or more carbon atoms and other copolymer components is preferably 8.0 mol% or less. When the copolymerization exceeds 8.0 mol%, the film may be whitened to have a poor appearance, or may become sticky and film formation may be difficult.
These resins may be used in a blend of two or more. When blending, individual resins may be copolymerized in excess of 8.0 mol%, but the blend is preferably monomer units and monomers other than propylene at 8.0 mol% or less. .
Further, as the polypropylene resin having a larger MFR, a polymer obtained by copolymerizing the above propylene and ethylene and / or an α-olefin having 4 or more carbon atoms can be used, or a propylene homopolymer can be used. I can do it. It is preferable to use a propylene homopolymer.
また、本発明の二軸配向ポリプロピレン系フィルムの表面層(B)のポリプロピレン系樹脂組成物は、MFRが1.0g/10分~8g/10分であることが好ましい。表面層(B)のポリプロピレン系樹脂組成物のMFRの下限は、2g/10分であることがより好ましく、3g/10分であることがさらに好ましい。表面層(B)のポリプロピレン系樹脂組成物のMFRの上限は、7g/10分であることがより好ましく、6.0g/10分であることがさらに好ましい。この範囲であると製膜性も良好で、外観にも優れる。
表面層(B)のポリプロピレン系樹脂組成物のMFRが1.0g/10分より小さいと、基材層(A)のポリプロピレン系樹脂のMFRが大きい場合に基材層(A)と表面層(B)の粘度差が大きくなるので、製膜の際にムラ(原反ムラ)が発生しやすくなる。表面層(B)のポリプロピレン系樹脂組成物のMFRが8g/10分を超えると、冷却ロールへの密着性が悪くなって、空気を巻き込み、平滑性が悪く、それが起点となる欠点が多くなって、適切な表面粗さになりにくいおそれがある。
In addition, the polypropylene resin composition of the surface layer (B) of the biaxially oriented polypropylene film of the present invention preferably has an MFR of 1.0 g / 10 min to 8 g / 10 min. The lower limit of the MFR of the polypropylene resin composition of the surface layer (B) is more preferably 2 g / 10 minutes, and further preferably 3 g / 10 minutes. The upper limit of the MFR of the polypropylene resin composition of the surface layer (B) is more preferably 7 g / 10 minutes, and further preferably 6.0 g / 10 minutes. Within this range, the film-forming property is good and the appearance is also excellent.
When the MFR of the polypropylene resin composition of the surface layer (B) is smaller than 1.0 g / 10 min, the base layer (A) and the surface layer ( Since the viscosity difference of B) becomes large, unevenness (raw fabric unevenness) is likely to occur during film formation. If the MFR of the polypropylene resin composition of the surface layer (B) exceeds 8 g / 10 minutes, the adhesion to the cooling roll will be poor, air will be involved, the smoothness will be poor, and there will be many drawbacks starting from it. Therefore, it may be difficult to obtain an appropriate surface roughness.
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の表面固有抵抗値は15LogΩ以上であることが好ましい。表面固有抵抗値は15LogΩ以上であると、印刷インキや接着剤との密着性が向上する。表面固有抵抗値は16LogΩ以上であるのがより好ましい。表面固有抵抗値は15LogΩ以上とするには、帯電防止剤、防曇剤などの低分子量化合物の添加剤を極力使用しないことが挙げられる。それを使用すると基材層(A)に含まれる添加剤が表面層(B)の基材層(A)とは反対側の表面にブリードしてくることもあり、それにより表面固有抵抗値が低下しにくくなるので、注意が必要である。
表面固有抵抗値を15LogΩ以上とするにはコロナ処理、火炎処理などの物理化学的な表面処理を行うことが好ましい。
例えば、コロナ処理では、予熱ロール、処理ロールを用い、空中で放電を行うことが好ましい。
It is preferable that the surface specific resistance value of the surface of the surface layer (B) of the biaxially oriented polypropylene film of the present invention on the side opposite to the base material layer (A) is 15 LogΩ or more. When the surface specific resistance value is 15 LogΩ or more, the adhesion to the printing ink and the adhesive is improved. The surface specific resistance value is more preferably 16 LogΩ or more. In order to make the surface specific resistance value 15 LogΩ or more, it is mentioned that an additive of a low molecular weight compound such as an antistatic agent or an antifogging agent is not used as much as possible. If it is used, the additive contained in the base material layer (A) may bleed to the surface of the surface layer (B) on the opposite side of the base material layer (A). Care must be taken because it is difficult to decrease.
In order to make the surface specific resistance value 15 LogΩ or more, it is preferable to perform physicochemical surface treatment such as corona treatment and flame treatment.
For example, in the corona treatment, it is preferable to discharge in the air using a preheating roll and a treatment roll.
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の濡れ張力が38mN/m以上であることが好ましい。濡れ張力は38mN/m以上であると、印刷インキや他部材フィルムとのラミネートに使用する接着剤との密着性が向上する。
濡れ張力を38mN/m以上とするには、帯電防止剤や界面活性剤などの添加剤を使用することが通常行われているが、これらの方法では、表面固有抵抗値を下げる効果があるため、コロナ処理、火炎処理などの物理化学的な表面処理を行うことが好ましい。
例えば、コロナ処理では、予熱ロール、処理ロールを用い、空中で放電を行うことが好ましい。
ここで表面固有抵抗値は主にコロナ処理の強さの程度と関係するが、濡れ張力は帯電防止剤のブリードアウト量とも関係するためそれぞれを好適な範囲にするのが効果的である。
It is preferable that the wetting tension of the surface opposite to the base material layer (A) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is 38 mN / m or more. When the wetting tension is 38 mN / m or more, the adhesiveness with the adhesive used for laminating with the printing ink or other member film is improved.
In order to increase the wetting tension to 38 mN / m or more, additives such as antistatic agents and surfactants are usually used. However, these methods have an effect of reducing the surface resistivity. It is preferable to perform physicochemical surface treatment such as corona treatment and flame treatment.
For example, in the corona treatment, it is preferable to discharge in the air using a preheating roll and a treatment roll.
Here, the surface specific resistance value is mainly related to the strength of the corona treatment, but the wetting tension is also related to the bleed-out amount of the antistatic agent, so it is effective to set each in a suitable range.
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の中心面山高さSR)+中心面谷深さSRvが1.0μm以上2.0μm以下であることが好ましい。
ここで、表面層(B)の基材層(A)とは反対側の表面の表面粗さ中心面山高さSRp、中心面谷深さSRvとは、三次元粗さ計を使用し、触針圧20mgにて、X方向の測定長さ1mm、Y方向の送りピッチ2μmで収録ライン数99本、高さ方向倍率20000倍、カットオフ80μmの測定を行い、JISB 0601(1994)に記載の算術平均粗さの定義に準じて、の求められる。
In the biaxially oriented polypropylene-based film of the present invention, the surface layer (B) has a center surface peak height SR) on the side opposite to the base material layer (A) and a center surface valley depth SRv of 1.0 μm or more and 2.0 μm. The following is preferable.
Here, the surface roughness of the surface layer (B) opposite to the base material layer (A) is the surface roughness center plane height SRp and the center plane valley depth SRv using a three-dimensional roughness meter. At a stylus pressure of 20 mg, a measurement length of 1 mm in the X direction, a feed pitch of 2 μm in the Y direction, 99 recording lines, a magnification in the height direction of 20000 times, and a cut-off of 80 μm were measured, as described in JISB 0601 (1994) According to the definition of arithmetic mean roughness,
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の中心面山高さSRp+中心面谷深さSRvは、アンチブロッキング剤などにより局所的に形成された比較的大きな凹凸の部分の状態の指標であり、例えば、基材層(A)と基材層(A)の少なくとも一方の表面に表面層(B)を有する本発明の二軸配向ポリプロピレン系フィルムをロール状に巻いたときに表面層(B)と基材層(A)とが接触した場合のそれらの間の滑り性に大きく関係するものである。
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の中心面山高さSRp+中心面谷深さSRvが1.0μm以上であると、ロールフィルムからの巻き出し性が向上し、2.0μm以下であると透明性が維持される。
表面層(B)の基材層(A)とは反対側の表面の中心面山高さSRp+中心面谷深さSRvは1.1μm以上が好ましく、1.2μm以上がより好ましく、1.3μm以上が特に好ましい。
The center plane peak height SRp + center plane valley depth SRv of the surface opposite to the base layer (A) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is locally increased by an antiblocking agent or the like. It is an indicator of the state of the relatively large irregularities formed, for example, the biaxial orientation of the present invention having a surface layer (B) on at least one surface of the substrate layer (A) and the substrate layer (A) This is largely related to the slipperiness between the surface layer (B) and the base material layer (A) when the polypropylene film is rolled up.
When the surface layer (B) of the biaxially oriented polypropylene film of the present invention has a center surface peak height SRp + center surface valley depth SRv of the surface opposite to the base layer (A) of 1.0 μm or more, a roll The unwinding property from a film improves and transparency is maintained as it is 2.0 micrometers or less.
The center plane peak height SRp + center plane valley depth SRv of the surface layer (B) opposite to the base material layer (A) is preferably 1.1 μm or more, more preferably 1.2 μm or more, and 1.3 μm or more. Is particularly preferred.
本発明の二軸配向ポリプロピレン系フィルムの表面層(B)の基材層(A)とは反対側の表面の中心面山高さSRp+中心面谷深さSRvが1.0μm以上2.0μm以下とするには、表面層(B)を形成するポリプロピレン系樹脂組成物にアンチブロッキング剤を配合するのが好適な方法である。
アンチブロッキング剤としては、シリカ、炭酸カルシウム、カオリン、ゼオライト等の無機系の粒子やアクリル系、ポリメタアクリル系、ポリスチレン系等の有機系の粒子の中から、適宜選択して使用することができる。これらの中でも、ポリメタアクリル系の粒子を用いるのが特に好ましい。アンチブロッキング剤の好ましい平均粒子径は1.0~2.5μmであり、より好ましくは1.0~2.0μmである。ここでいう平均粒径の測定法は、走査電子顕微鏡で写真撮影し、イメージアナライザー装置を用いて水平方向のフェレ径を測定し、その平均値で表示したものである。
アンチブロッキング剤は、ポリプロピレン樹脂あるいはその混合物全体に対して中0.15質量%とすることが好ましい。
The center plane peak height SRp + center plane valley depth SRv of the surface opposite to the base layer (A) of the surface layer (B) of the biaxially oriented polypropylene film of the present invention is 1.0 μm or more and 2.0 μm or less. For this purpose, an antiblocking agent is preferably added to the polypropylene resin composition forming the surface layer (B).
As the anti-blocking agent, it can be appropriately selected from inorganic particles such as silica, calcium carbonate, kaolin and zeolite, and organic particles such as acrylic, polymethacrylic and polystyrene. . Among these, it is particularly preferable to use polymethacrylic particles. The average particle size of the antiblocking agent is preferably 1.0 to 2.5 μm, more preferably 1.0 to 2.0 μm. The measurement method of the average particle diameter here is a method in which a photograph is taken with a scanning electron microscope, the ferret diameter in the horizontal direction is measured using an image analyzer, and the average value is displayed.
The antiblocking agent is preferably 0.15% by mass relative to the entire polypropylene resin or mixture thereof.
本発明で用いるポリプロピレン系樹脂は、チーグラー・ナッタ触媒やメタロセン触媒等の公知の触媒を用いて、原料のプロピレンを単独で重合させること、あるいはプロピレンとエチレン及び/又はα-オレフィンを共重合することにより得られる。中でも、異種結合をなくすためにはチーグラー・ナッタ触媒を用い、立体規則性の高い重合が可能な触媒を用いることが好ましい。
重合方法としては、公知の方法を採用すればよく、例えば、ヘキサン、ヘプタン、トルエン、キシレン等の不活性溶剤中で重合する方法、液状のモノマー中で重合する方法、気体のモノマーに触媒を添加し、気相状態で重合する方法、または、これらを組み合わせて重合する方法等が挙げられる。
The polypropylene resin used in the present invention is a polymer of propylene as a raw material alone or a copolymer of propylene and ethylene and / or α-olefin using a known catalyst such as a Ziegler-Natta catalyst or a metallocene catalyst. Is obtained. Among these, in order to eliminate the heterogeneous bond, it is preferable to use a Ziegler-Natta catalyst and a catalyst capable of polymerization with high stereoregularity.
As a polymerization method, a known method may be employed, for example, a method of polymerizing in an inert solvent such as hexane, heptane, toluene, xylene, a method of polymerizing in a liquid monomer, or adding a catalyst to a gaseous monomer. And the method of superposing | polymerizing in a gaseous-phase state, the method of superposing | polymerizing combining these, etc. are mentioned.
本発明の本発明の二軸配向ポリプロピレン系フィルムの基材層(A)には、添加剤やその他の樹脂を含有させてもよい。添加剤としては、例えば、酸化防止剤、紫外線吸収剤、造核剤、粘着剤、防曇剤、難燃剤、無機または有機の充填剤等が挙げられる。
その他の樹脂としては、本発明で用いられるポリプロピレン樹脂以外のポリプロピレン樹脂、プロピレンとエチレンおよび/または炭素数4以上のα-オレフィンとの共重合体であるランダムコポリマーや、各種エラストマー等が挙げられる。これらは、多段の反応器を用いて逐次重合するか、ポリプロピレン樹脂とヘンシェルミキサーでブレンドするか、事前に溶融混錬機を用いて作製したマスターペレットを所定の濃度になるようにポリプロピレンで希釈するか、予め全量を溶融混練して使用してもよい。
基材層(B)には、添加剤やその他の樹脂を含有させてもよい。添加剤としては、例えば、酸化防止剤、紫外線吸収剤、造核剤、粘着剤、防曇剤、難燃剤、無機または有機の充填剤等が挙げられる。
The base layer (A) of the biaxially oriented polypropylene film of the present invention of the present invention may contain additives and other resins. Examples of the additive include an antioxidant, an ultraviolet absorber, a nucleating agent, an adhesive, an antifogging agent, a flame retardant, and an inorganic or organic filler.
Examples of the other resin include polypropylene resins other than the polypropylene resin used in the present invention, random copolymers that are copolymers of propylene and ethylene and / or α-olefins having 4 or more carbon atoms, and various elastomers. These are sequentially polymerized using a multistage reactor, blended with a polypropylene resin and a Henschel mixer, or master pellets prepared in advance using a melt kneader are diluted with polypropylene to a predetermined concentration. Alternatively, the whole amount may be melt kneaded in advance.
The base material layer (B) may contain additives and other resins. Examples of the additive include an antioxidant, an ultraviolet absorber, a nucleating agent, an adhesive, an antifogging agent, a flame retardant, and an inorganic or organic filler.
(3)二軸配向ポリプロピレン系フィルム
本発明の二軸配向ポリプロピレン系フィルムは、基材層(A)と表面層(B)とを1層ずつ有する2層構造のフィルムであってもよいが3層以上の構成としてもよい。好ましいのは基材層(A)/表面層(B)の2層構造であるが、表面層(B)/A層/表面層(B)、/基材層(A)/中間層(C)/表面層(B)の3層構造やそれ以上の多層構造であってもよい。
なお、基材層(A)や表面層(B)が複数ある場合、それぞれの層がその特性を満たすものであれば、組成は異なっていてもよい。
本発明の二軸配向ポリプロピレン系フィルム全体の厚みは9~200mが好ましく、10~150μmがより好ましく、12~100μmがさらに好ましく、12~80μmが特に好ましい。
(3) Biaxially oriented polypropylene film The biaxially oriented polypropylene film of the present invention may be a film having a two-layer structure having a base layer (A) and a surface layer (B) one by one. It is good also as a structure more than a layer. Preferred is a two-layer structure of substrate layer (A) / surface layer (B), but surface layer (B) / A layer / surface layer (B), / substrate layer (A) / intermediate layer (C). ) / Surface layer (B) three-layer structure or more than that.
In addition, when there are a plurality of substrate layers (A) and surface layers (B), the compositions may be different as long as each layer satisfies the characteristics.
The total thickness of the biaxially oriented polypropylene film of the present invention is preferably 9 to 200 m, more preferably 10 to 150 μm, still more preferably 12 to 100 μm, and particularly preferably 12 to 80 μm.
本発明の二軸配向ポリプロピレン系フィルムにおける表面層(B)全体の厚みと基材層(A)の厚みの比率としては、表面層(B)全体の厚み/基材層(A)の厚みが0.01~0.5であることが好ましく、0.02~0.4であることがより好ましく、0.03~0.3であることがさらに好ましい。全表面層(B)/全基材層(A)が0.5を超えると、収縮率が大きくなる傾向を示す。また、フィルム全体の厚みに対する全基材層(A)の厚みは50~99%であることが好ましく、さらに好ましくは60~97%、特に好ましくは70~95%である。残部は、表面層(B)または表面層(B)と中間層(C)となる。全表面層(B)の実質的な厚みは、0.5~4μmが好ましく、1~3.5μmがより好ましく、1.5~3μmがさらに好ましい。 As the ratio of the thickness of the entire surface layer (B) and the thickness of the base material layer (A) in the biaxially oriented polypropylene film of the present invention, the thickness of the entire surface layer (B) / the thickness of the base material layer (A) is It is preferably from 0.01 to 0.5, more preferably from 0.02 to 0.4, and even more preferably from 0.03 to 0.3. When the total surface layer (B) / total base material layer (A) exceeds 0.5, the shrinkage rate tends to increase. The total thickness of the base layer (A) is preferably 50 to 99%, more preferably 60 to 97%, and particularly preferably 70 to 95% with respect to the total thickness of the film. The remainder becomes the surface layer (B) or the surface layer (B) and the intermediate layer (C). The substantial thickness of the entire surface layer (B) is preferably 0.5 to 4 μm, more preferably 1 to 3.5 μm, and even more preferably 1.5 to 3 μm.
本発明の二軸配向ポリプロピレン系フィルムのインキ密着性の評価は、グラビア印刷した印刷インキの剥離試験を行い、全体25箇所のうち、剥離する部分の個数で行った。剥離箇所が5個以下が好ましく、3個以下がより好ましく、0個が最も好ましい。5個を超えると、印刷インキの剥がれる程度が大きくなり問題である。インキ密着性の評価方法は後述する。 The evaluation of the ink adhesion of the biaxially oriented polypropylene film of the present invention was carried out by performing a peel test of gravure-printed printing ink and performing the number of peeled portions out of the total 25 locations. The number of peeled portions is preferably 5 or less, more preferably 3 or less, and most preferably 0. If the number exceeds 5, the degree to which the printing ink peels becomes large, which is a problem. A method for evaluating ink adhesion will be described later.
本発明の二軸配向ポリプロピレン系フィルムへのラミネート後の縦方向のラミネート強度は、1.2~2.5N/15mmが好ましく、1.3~2.5N/mmがより好ましく、1.4~2.5N/mmがさらに好ましい。ラミネート強度の測定方法は後述する。 The lamination strength in the longitudinal direction after lamination to the biaxially oriented polypropylene film of the present invention is preferably 1.2 to 2.5 N / 15 mm, more preferably 1.3 to 2.5 N / mm, and 1.4 to 2.5 N / mm is more preferable. A method for measuring the laminate strength will be described later.
本発明の二軸配向ポリプロピレン系フィルムの動摩擦係数は、0.5以下であることが好ましく、0.48以下であるのがより好ましく、0.45以下が特にこのましい。動摩擦係数は、0.5以下であるとロールフィルムからのフィルムの巻き出しがスムーズに行え、印刷加工しやすい。動摩擦係数の測定方法は後述する。 The dynamic friction coefficient of the biaxially oriented polypropylene film of the present invention is preferably 0.5 or less, more preferably 0.48 or less, and particularly preferably 0.45 or less. When the dynamic friction coefficient is 0.5 or less, the film can be smoothly unwound from the roll film, and printing is easy. A method for measuring the dynamic friction coefficient will be described later.
本発明の二軸配向ポリプロピレン系フィルムのヘイズは、5%以下が好ましく、0.2~5%がより好ましく、0.3~4.5%がさらに好ましく、0.4~4%が特に好ましい。5%を超えると透明性に劣り、印刷された表示が見にくくなることがある。ヘイズは例えば延伸温度、熱固定温度が高すぎる場合、冷却ロール温度が高く未延伸(原反)シートの冷却速度が遅い場合、低分子量成分が多すぎる場合に悪くなる傾向があり、これらを調節することで上記の範囲内とすることが出来る。ヘイズの測定方法は後述する。 The haze of the biaxially oriented polypropylene film of the present invention is preferably 5% or less, more preferably 0.2 to 5%, further preferably 0.3 to 4.5%, and particularly preferably 0.4 to 4%. . If it exceeds 5%, the transparency is inferior and the printed display may be difficult to see. For example, when the stretching temperature and heat setting temperature are too high, the haze tends to be worse when the cooling roll temperature is high, the cooling rate of the unstretched (raw material) sheet is slow, or when there are too many low molecular weight components. By doing so, it can be within the above range. A method for measuring haze will be described later.
本発明の二軸配向二軸配向ポリプロピレン系フィルムの縦方向および横方向の150℃での熱収縮率が11%以下であることが好ましく、10%以下であることがより好ましく、8%以下であることが特に好ましい。熱収縮率が11%以下とすることで、印刷時のピッチずれを低減することができる。熱収縮の測定方法は後述する。 The biaxially oriented biaxially oriented polypropylene film of the present invention preferably has a heat shrinkage rate of 150% at 150 ° C. in the machine direction and the transverse direction, preferably 10% or less, more preferably 8% or less. It is particularly preferred. By setting the thermal shrinkage rate to 11% or less, it is possible to reduce the pitch deviation during printing. A method for measuring thermal shrinkage will be described later.
本発明の二軸配向ポリプロピレン系フィルムにおいては、150℃での縦方向の熱収縮率は0.2~8%であることが好ましく、0.3~7%がより好ましく、0.5~6%であることが特に好ましい。熱収縮率が上記範囲であれば、耐熱性に優れたフィルムということができ、高温にさらされる可能性のある用途でも使用できる。なお、150℃熱収縮率は1.5%程度までなら、例えば低分子量成分を多くする、延伸条件、熱固定条件を調整することで可能であるが、それ以下に下げるには、オフラインでアニール処理をすること等が好ましい。 In the biaxially oriented polypropylene film of the present invention, the thermal shrinkage in the longitudinal direction at 150 ° C. is preferably 0.2 to 8%, more preferably 0.3 to 7%, and more preferably 0.5 to 6 % Is particularly preferred. If the heat shrinkage rate is in the above range, it can be said that the film has excellent heat resistance, and can be used in applications that may be exposed to high temperatures. If the thermal shrinkage at 150 ° C. is up to about 1.5%, for example, it is possible to increase the low molecular weight component, adjust the stretching conditions and the heat setting conditions, but in order to lower it below, anneal offline. It is preferable to perform the treatment.
本発明の二軸配向ポリプロピレン系フィルムの縦方向の引張弾性率は、1.8~4GPaであることが好ましく、2.1~3.7GPaであることがより好ましく、2.2~3.5GPaであることがさらに好ましく、2.3~3.4GPaが特に好ましい。横方向の引張弾性率は、3.8~8GPaであることが好ましく、4~7.5GPaであることがより好ましく、4.1~7GPaであることがさらに好ましく、4.2~6.5GPaが特に好ましい。引張弾性率が上記範囲であれば、腰が強くなり、フィルム厚みが小さくても使用できるため、フィルムの使用量を減らすことが可能となる。引張弾性率の測定方法は後述する。 The tensile modulus in the machine direction of the biaxially oriented polypropylene film of the present invention is preferably 1.8 to 4 GPa, more preferably 2.1 to 3.7 GPa, and 2.2 to 3.5 GPa. Is more preferable, and 2.3 to 3.4 GPa is particularly preferable. The tensile modulus in the transverse direction is preferably 3.8 to 8 GPa, more preferably 4 to 7.5 GPa, still more preferably 4.1 to 7 GPa, and 4.2 to 6.5 GPa. Is particularly preferred. If the tensile elastic modulus is in the above range, the elasticity becomes strong and the film can be used even if the film thickness is small, so the amount of film used can be reduced. A method for measuring the tensile modulus will be described later.
本発明の二軸配向ポリプロピレン系フィルムの面配向係数の下限は、0.011が好ましく、0.012がより好ましく、0.013がさらに好ましい。上記範囲であると、フィルムの耐熱性、剛性を大きくなりやすい。
延伸された積層ポリプロピレン系フィルムは、一般的に結晶配向を有し、その方向や程度がフィルム物性に大きな影響を及ぼす。結晶配向の程度は、用いられるポリプロピレン系樹脂の分子構造や、フィルム製造におけるプロセスや条件によって変化する傾向であり、これらを調節することで上記の範囲内とすることが出来る。面配向係数の測定方法は後述する。
The lower limit of the plane orientation coefficient of the biaxially oriented polypropylene film of the present invention is preferably 0.011, more preferably 0.012, and even more preferably 0.013. Within the above range, the heat resistance and rigidity of the film tend to increase.
The stretched laminated polypropylene film generally has a crystal orientation, and its direction and degree greatly affect the film properties. The degree of crystal orientation tends to change depending on the molecular structure of the polypropylene resin used and the process and conditions in film production, and can be adjusted to the above range by adjusting these. A method for measuring the plane orientation coefficient will be described later.
(4)製膜方法
本発明の二軸配向ポリプロピレン系フィルムは、基材層(A)用ポリプロピレン系樹脂組成物と表面層(B)用ポリプロピレン系樹脂組成物を別々の押出機により溶融押し出しし、ダイスから共押出しして、冷却ロールで冷却して、未延伸シートを形成し、その未延伸シートを縦方向(MD)及び幅方向(TD)に延伸した後、熱固定処理することによって得ることができる。
溶融押出し温度は200~280℃程度が好ましく、この温度範囲内で層を乱さずに良好な外観の積層フィルムを得るには、基材層(A)用ポリプロピレン原料と表面層(B)用ポリプロピレン原料の粘度差(MFR差)が6g/10分以下となるようにすることが好ましい。粘度差が6g/10分より大きいと、層が乱れて外観不良となりやすい。より好ましくは5.5g/10分以下、さらに好ましくは5g/10分以下である。
(4) Film-forming method The biaxially oriented polypropylene film of the present invention is obtained by melt-extruding the polypropylene resin composition for the base layer (A) and the polypropylene resin composition for the surface layer (B) by separate extruders. It is obtained by co-extrusion from a die, cooling with a cooling roll to form an unstretched sheet, stretching the unstretched sheet in the machine direction (MD) and the width direction (TD), and then heat setting. be able to.
The melt extrusion temperature is preferably about 200 to 280 ° C. In order to obtain a laminated film having a good appearance without disturbing the layer within this temperature range, the polypropylene raw material for the base layer (A) and the polypropylene for the surface layer (B) The viscosity difference (MFR difference) of the raw materials is preferably 6 g / 10 minutes or less. When the viscosity difference is larger than 6 g / 10 min, the layer is disturbed and the appearance is liable to be poor. More preferably, it is 5.5 g / 10 minutes or less, More preferably, it is 5 g / 10 minutes or less.
冷却ロール表面温度は25~35℃が好ましく、27~33℃がより好ましい。温度が35℃を超えるとフィルム表面が荒れやすくなる。 The surface temperature of the cooling roll is preferably 25 to 35 ° C, more preferably 27 to 33 ° C. When the temperature exceeds 35 ° C., the film surface tends to be rough.
縦方向(MD)の延伸倍率の下限は、好ましくは3倍であり、より好ましくは3.5倍である。上記未満であると膜厚ムラとなることがある。MDの延伸倍率の上限は好ましくは8倍であり、より好ましくは7倍である。上記を超えると引き続き行うTD延伸がしにくくなることがある。MDの延伸温度の下限は好ましくは120℃であり、より好ましくは125℃であり、さらに好ましくは130℃である。上記未満であると機械的負荷が大きくなったり、厚みムラが大きくなったり、フィルムの表面荒れが起こることがある。MDの延伸温度の上限は好ましくは150℃であり、より好ましくは145℃であり、さらに好ましくは140℃である。温度が高い方が熱収縮率の低下には好ましいが、ロールに付着し延伸できなくなったり、表面荒れが起こることがある。 The lower limit of the draw ratio in the machine direction (MD) is preferably 3 times, more preferably 3.5 times. If it is less than the above, film thickness unevenness may occur. The upper limit of the MD draw ratio is preferably 8 times, more preferably 7 times. When the above is exceeded, it may be difficult to carry out TD stretching continuously. The lower limit of the MD stretching temperature is preferably 120 ° C, more preferably 125 ° C, and even more preferably 130 ° C. If it is less than the above, the mechanical load may increase, the thickness unevenness may increase, or the film surface may be roughened. The upper limit of the MD stretching temperature is preferably 150 ° C, more preferably 145 ° C, and further preferably 140 ° C. A higher temperature is preferable for lowering the thermal shrinkage, but it may adhere to the roll and cannot be stretched, or surface roughness may occur.
幅方向(TD)の延伸倍率の下限は好ましくは4倍であり、より好ましくは5倍であり、さらに好ましくは6倍である。上記未満であると厚みムラとなることがある。TD延伸倍率の上限は好ましくは20倍であり、より好ましくは17倍であり、さらに好ましくは15倍であり、特に好ましくは12倍である。上記を超えると熱収縮率が高くなったり、延伸時に破断することがある。TD延伸での予熱温度は速やかに延伸温度付近にフィルム温度を上げるため、好ましくは延伸温度より5~15℃高く設定する。TDの延伸では従来の延伸ポリプロピレン系フィルムより高温で行う。TDの延伸温度の下限は好ましくは155℃であり、より好ましくは157℃であり、さらに好ましくは158℃、特に好ましくは160℃である。上記未満であると充分に軟化せずに破断したり、熱収縮率が高くなることがある。TD延伸温度の上限は好ましくは170℃であり、より好ましくは168℃であり、さらに好ましくは163℃である。熱収縮率を低くするためには温度は高い方が好ましいが、上記を超えると低分子成分が融解、再結晶化して配向が低下するだけでなく、表面荒れやフィルムが白化することがある。 The lower limit of the draw ratio in the width direction (TD) is preferably 4 times, more preferably 5 times, and even more preferably 6 times. If it is less than the above, thickness unevenness may occur. The upper limit of the TD stretch ratio is preferably 20 times, more preferably 17 times, still more preferably 15 times, and particularly preferably 12 times. If the above is exceeded, the thermal shrinkage rate may be increased or the film may be broken during stretching. The preheating temperature in TD stretching is preferably set to 5 to 15 ° C. higher than the stretching temperature in order to quickly raise the film temperature in the vicinity of the stretching temperature. The TD stretching is performed at a higher temperature than the conventional stretched polypropylene film. The lower limit of the TD stretching temperature is preferably 155 ° C, more preferably 157 ° C, still more preferably 158 ° C, and particularly preferably 160 ° C. If it is less than the above, it may break without being sufficiently softened, or the thermal shrinkage rate may be increased. The upper limit of the TD stretching temperature is preferably 170 ° C, more preferably 168 ° C, and further preferably 163 ° C. In order to lower the thermal shrinkage rate, it is preferable that the temperature is higher. However, if the temperature is higher than the above, the low molecular component is melted and recrystallized to lower the orientation, and the surface may be roughened or the film may be whitened.
延伸後のフィルムは熱固定される。熱固定は従来の延伸ポリプロピレン系フィルムより高温で行うことが可能である。熱固定温度の下限は好ましくは165℃であり、より好ましくは166℃である。上記未満であると熱収縮率が高くなることがある。また、熱収縮率を低くするために長時間の処理が必要になり、生産性が劣ることがある。熱固定温度の上限は好ましくは176℃であり、より好ましくは175℃である。上記を超えると低分子成分が融解、再結晶化して表面荒れやフィルムが白化することがある。 The stretched film is heat-set. The heat setting can be performed at a higher temperature than a conventional stretched polypropylene film. The lower limit of the heat setting temperature is preferably 165 ° C, more preferably 166 ° C. If it is less than the above, the thermal shrinkage rate may increase. In addition, a long time treatment is required to lower the heat shrinkage rate, and productivity may be inferior. The upper limit of the heat setting temperature is preferably 176 ° C, more preferably 175 ° C. When the above is exceeded, the low molecular component may melt and recrystallize, and the surface roughness or the film may be whitened.
熱固定時には緩和(リラックス)させることが好ましい。緩和(リラックス)の下限は好ましくは2%であり、より好ましくは3%である。上記未満であると熱収縮率が高くなることがある。緩和(リラックス)の上限は好ましくは10%であり、より好ましくは8%である。上記を超えると厚みムラが大きくなることがある。 It is preferable to relax (relax) during heat setting. The lower limit of relaxation (relaxation) is preferably 2%, more preferably 3%. If it is less than the above, the thermal shrinkage rate may increase. The upper limit of relaxation (relaxation) is preferably 10%, more preferably 8%. When the above is exceeded, the thickness unevenness may increase.
さらに、熱収縮率を低下させるために、上記の工程で製造されたフィルムを一旦ロール状に巻き取った後、オフラインでアニールさせることもできる。オフラインアニールの温度の下限は好ましくは160℃であり、より好ましくは162℃であり、さらに好ましくは163℃である。上記未満であるとアニールの効果が得られないことがある。オフラインアニール温度の上限は好ましくは175℃であり、より好ましくは174℃であり、さらに好ましくは173℃である。上記を超えると透明性が低下したり、厚みムラが大きくなったりすることがある。 Furthermore, in order to reduce the thermal shrinkage rate, the film produced in the above process can be once wound into a roll and then annealed offline. The lower limit of the offline annealing temperature is preferably 160 ° C, more preferably 162 ° C, and even more preferably 163 ° C. If it is less than the above, the effect of annealing may not be obtained. The upper limit of the offline annealing temperature is preferably 175 ° C., more preferably 174 ° C., and further preferably 173 ° C. When the above is exceeded, the transparency may decrease, or the thickness unevenness may increase.
オフラインアニール時間の下限は好ましくは0.1分であり、より好ましくは0.5分であり、さらに好ましくは1分である。上記未満であるとアニールの効果が得られないことがある。オフラインアニール時間の上限は好ましくは30分であり、より好ましくは25分であり、さらに好ましくは20分である。上記を超えると生産性が低下することがある。 The lower limit of the offline annealing time is preferably 0.1 minutes, more preferably 0.5 minutes, and even more preferably 1 minute. If it is less than the above, the effect of annealing may not be obtained. The upper limit of the offline annealing time is preferably 30 minutes, more preferably 25 minutes, and further preferably 20 minutes. When the above is exceeded, productivity may be reduced.
こうして得られた二軸配向ポリプロピレン系フィルムに、必要に応じて、コロナ放電、プラズマ処理、火炎処理等を施した後、ワインダーで巻き取ることにより本発明の二軸配向ポリプロピレンフィルムロールを得ることができる。 The biaxially oriented polypropylene film thus obtained can be subjected to corona discharge, plasma treatment, flame treatment, etc., if necessary, and then wound with a winder to obtain the biaxially oriented polypropylene film roll of the present invention. it can.
本発明の二軸配向ポリプロピレン系フィルムは、例えば、そのために印刷インキやラミネート等の加工がなされる用途に広く使用することができる。 The biaxially oriented polypropylene film of the present invention can be widely used, for example, for applications in which processing such as printing ink or lamination is performed.
以下、実施例によって本発明をさらに詳述するが、下記実施例は本発明を制限するものではなく、本発明の趣旨を逸脱しない範囲で変更実施する場合は、本発明に含まれる。 Hereinafter, the present invention will be described in more detail by way of examples. However, the following examples are not intended to limit the present invention, and modifications and implementations without departing from the spirit of the present invention are included in the present invention.
(測定方法)
実施例および比較例で得られたフィルム物性の測定方法は、以下の通りである。
(Measuring method)
The measuring method of the film physical property obtained by the Example and the comparative example is as follows.
1)立体規則性
メソペンタッド分率([mmmm]%)の測定は、13C-NMRを用いて行った。メソペンタッド分率は、「Zambelliら、Macromolecules,第6巻,925頁(1973)」に記載の方法に従って算出した。13C-NMR測定は、BRUKER社製「AVANCE500」を用い、試料200mgをo-ジクロロベンゼンと重ベンゼンの8:2(体積比)の混合液に135℃で溶解し、110℃で行った。
1) Stereoregularity The mesopentad fraction ([mmmm]%) was measured using 13C-NMR. The mesopentad fraction was calculated according to the method described in “Zambelli et al., Macromolecules, Vol. 6, 925 (1973)”. The 13C-NMR measurement was performed at 110 ° C. by using “AVANCE 500” manufactured by BRUKER, and dissolving 200 mg of a sample in an 8: 2 (volume ratio) mixture of o-dichlorobenzene and heavy benzene at 135 ° C.
2)メルトフローレート(MFR;g/10分)
JIS K7210に準拠し、温度230℃、荷重2.16kgfで測定した。
原料樹脂の場合はペレット(パウダー)をそのまま必要量を秤り取って用いた。フィルムの場合は必要量切り出した後、約5mm角にカットしたサンプルを用いた。
2) Melt flow rate (MFR; g / 10 min)
According to JIS K7210, the temperature was 230 ° C. and the load was 2.16 kgf.
In the case of a raw material resin, pellets (powder) were used as they were by weighing out the required amount. In the case of a film, after cutting out a necessary amount, a sample cut into about 5 mm square was used.
3)分子量および分子量分布
原料樹脂及びフィルムの分子量および分子量分布は、ゲルパーミエーションクロマトグラフィー(GPC)を用いて単分散ポリスチレン基準により求めた。GPC測定での使用カラム、溶媒等の測定条件は以下のとおりである。
溶媒:1,2,4-トリクロロベンゼン
カラム:TSKgel GMHHR-H(20)HT×3
流量:1.0ml/min
検出器:RI
測定温度:140℃
3) Molecular weight and molecular weight distribution The molecular weight and molecular weight distribution of the raw resin and film were determined on the basis of monodisperse polystyrene using gel permeation chromatography (GPC). The measurement conditions such as the column used and the solvent in GPC measurement are as follows.
Solvent: 1,2,4-trichlorobenzene Column: TSKgel GMHHR-H (20) HT × 3
Flow rate: 1.0 ml / min
Detector: RI
Measurement temperature: 140 ° C
数平均分子量(Mn)、質量平均分子量(Mw)、分子量分布は、それぞれ、分子量校正曲線を介して得られたGPC曲線の各溶出位置の分子量(Mi)の分子数(Ni)により次式で定義される。
数平均分子量:Mn=Σ(Ni・Mi)/ΣNi
質量平均分子量:Mw=Σ(Ni・Mi
2)/Σ(Ni・Mi)
分子量分布:Mw/Mn
ベースラインが明確でないときは、標準物質の溶出ピークに最も近い高分子量側の溶出ピークの高分子量側のすそ野の最も低い位置までの範囲でベースラインを設定することとした。
The number average molecular weight (Mn), the mass average molecular weight (Mw), and the molecular weight distribution are respectively represented by the molecular number (N i ) of the molecular weight (M i ) at each elution position of the GPC curve obtained through the molecular weight calibration curve. It is defined by an expression.
Number average molecular weight: Mn = Σ (N i · M i ) / ΣN i
Mass average molecular weight: Mw = Σ (N i · M i 2 ) / Σ (N i · M i )
Molecular weight distribution: Mw / Mn
When the baseline was not clear, the baseline was set in the range from the elution peak closest to the elution peak of the standard substance to the lowest position of the bottom of the high molecular weight side.
4)厚み
基材層(A)と表面層(B)各層の厚みは、二軸延伸積層ポリプロピレン系フィルムを変性ウレタン樹脂で固めたものの断面をミクロトームで切り出し、微分干渉顕微鏡で観察して、測定した。
4) Thickness The thickness of each of the base layer (A) and the surface layer (B) is measured by cutting a cross section of a biaxially stretched laminated polypropylene film hardened with a modified urethane resin with a microtome and observing with a differential interference microscope. did.
5)熱収縮率(%)
JIS Z1712に準拠して、以下の方法で測定した。フィルムを、MD方向とTD方向のそれぞれにおいて、幅20mm、長さ200mmにカットし、150℃の熱風オーブン中に吊して5分間加熱した。加熱前後の長さを測定し、加熱前の長さから加熱後の長さを引いた長さをの加熱前の長さに対する割合(%)を求め、熱収縮率を求めた。
5) Thermal shrinkage (%)
Based on JIS Z1712, it measured by the following method. The film was cut into a width of 20 mm and a length of 200 mm in each of the MD direction and the TD direction, suspended in a hot air oven at 150 ° C. and heated for 5 minutes. The length before and after heating was measured, the ratio (%) of the length obtained by subtracting the length after heating from the length before heating to the length before heating was determined, and the thermal shrinkage rate was determined.
6)引張弾性率(GPa)
JIS K7127に準拠してフィルムのMD方向およびTD方向の引張弾性率を23℃にて、下記条件で測定した。
測定機器:島津製作所、オートグラフ ASS-100NJ
サンプルサイズ:幅15mm×長さ200mm
クロスヘッド速度:200mm/min
チャック間距離:100mm
弾性率測定の歪範囲:0.1~0.6%
6) Tensile modulus (GPa)
Based on JIS K7127, the tensile elastic modulus in the MD direction and TD direction of the film was measured at 23 ° C. under the following conditions.
Measuring equipment: Shimadzu Corporation, Autograph ASS-100NJ
Sample size: width 15mm x length 200mm
Crosshead speed: 200mm / min
Distance between chucks: 100mm
Elasticity measurement strain range: 0.1-0.6%
7)ヘイズ(単位:%)
JIS K7105に従って測定した。
7) Haze (Unit:%)
It measured according to JIS K7105.
8)動摩擦係数
JIS K7125に準拠して、2枚のフィルムの表面層(B)面同士を重ね合わせ、23℃で測定した。
8) Coefficient of dynamic friction According to JIS K7125, the surface layer (B) surfaces of two films were superposed and measured at 23 ° C.
9)屈折率、面配向係数
JIS K7142-1996 5.1(A法)により、アタゴ製アッベ屈折計を用いて測定した。MD、TD方向に沿った屈折率をそれぞれNx、Nyとし、厚み方向の屈折率をNzとした。面配向係数(ΔP)は、(Nx+Ny)/2-Nzで求めた。
9) Refractive index, plane orientation coefficient Measured using an Atago Abbe refractometer according to JIS K7142-1996 5.1 (Method A). The refractive indexes along the MD and TD directions were Nx and Ny, respectively, and the refractive index in the thickness direction was Nz. The plane orientation coefficient (ΔP) was determined by (Nx + Ny) / 2−Nz.
10)表面粗さ
得られたフィルムの表面粗さ評価は、三次元粗さ計(小坂研究所社製、型番ET-30HK)を使用し、触針圧20mgにて、X方向の測定長さ1mm、送り速さ100μm/秒、Y方向の送りピッチ2μmで収録ライン数99本、高さ方向倍率20000倍、カットオフ80μmの測定を行い、JISB 0601(1994)に記載の算術平均粗さの定義に準じて、計算した。
算術平均粗さ(SRa)、中心面山高さ(SRp)、及び中心面谷深さ(SRv)はそれぞれ3回の試行を行い、その平均値で評価した。
10) Surface roughness The surface roughness of the obtained film was evaluated using a three-dimensional roughness meter (manufactured by Kosaka Laboratories, model number ET-30HK) at a stylus pressure of 20 mg and measured length in the X direction. 1 mm, feed speed 100 μm / second, Y-direction feed pitch 2 μm, 99 recording lines, height direction magnification 20000 times, cut-off 80 μm were measured, and the arithmetic average roughness described in JISB 0601 (1994) was measured. Calculated according to the definition.
Arithmetic average roughness (SRa), center plane mountain height (SRp), and center plane valley depth (SRv) were each evaluated three times and evaluated by their average values.
11)表面固有抵抗値(LogΩ)
JIS K6911に準拠し、フィルムを23℃、24時間エージング後、フィルムの表面層(B)面を測定した。
11) Surface resistivity (LogΩ)
In accordance with JIS K6911, the surface layer (B) surface of the film was measured after aging the film at 23 ° C. for 24 hours.
12)濡れ張力(mN/m)
K 6768 : 1999に順じて、フィルムを23℃、相対湿度 50%で24時間エージング後、下記手順でフィルムのコロナ処理面を測定した。
手順1)
測定は,温度 23℃,相対湿度 50%の標準試験室雰囲気(JIS K 7100 参照)で行う。
手順2)
試験片をハンドコータ(4.1)の基板の上に置き、試験片の上に試験用混合液を数滴滴下して、直ちにワイヤバーを引いて広げる。
綿棒又はブラシを使用して試験用混合液を広げる場合は、液体は少なくとも6cm2以上の面積に速やかに広げる。液体の量は、たまりを作らないで、薄層を形成する程度にする。
濡れ張力の判定は,試験用混合液の液膜を明るいところで観察し、3秒後の液膜の状態で行う。液膜破れを生じないで、3秒以上、塗布されたときの状態を保っているのは、ぬれていることになる。濡れが3秒以上保つ場合は、さらに、次に表面張力の高い混合液に進み、また逆に、3秒以下で液膜が破れる場合は、次の表面張力の低い混合液に進む。
この操作を繰り返し、試験片の表面を正確に、3秒間で濡らすことができる混合液を選ぶ。
手順3)
各々の試験には,新しい綿棒を使用する。ブラシ又はワイヤバーは,残留する液体が蒸発によって組成及び表面張力を変化させるので、使用ごとにメタノールで洗浄し、乾燥させる。
手順4)
試験片の表面を3秒間でぬらすことができる混合液を選ぶ操作を少なくとも3回行う。このようにして選ばれた混合液の表面張力をフィルムの濡れ張力として報告する。
12) Wetting tension (mN / m)
In accordance with K6768: 1999, the film was aged for 24 hours at 23 ° C. and 50% relative humidity, and then the corona-treated surface of the film was measured by the following procedure.
Procedure 1)
The measurement is performed in a standard laboratory atmosphere (see JIS K 7100) at a temperature of 23 ° C and a relative humidity of 50%.
Step 2)
Place the test piece on the substrate of the hand coater (4.1), drop a few drops of the test mixture on the test piece and immediately pull the wire bar to spread.
When using a cotton swab or brush to spread the test mixture, the liquid is quickly spread over an area of at least 6 cm2. The amount of liquid is such that a thin layer is formed without creating a pool.
The wet tension is determined by observing the liquid film of the test liquid mixture in a bright place and in the liquid film state after 3 seconds. It is wet to maintain the state when applied for 3 seconds or more without causing the liquid film to break. When the wetting is maintained for 3 seconds or more, the process proceeds to a liquid mixture having the next highest surface tension. Conversely, when the liquid film is broken within 3 seconds or less, the process proceeds to the next liquid mixture having a low surface tension.
This operation is repeated, and a liquid mixture that can accurately wet the surface of the test piece in 3 seconds is selected.
Step 3)
Use a new swab for each test. The brush or wire bar is washed with methanol and dried after each use because the remaining liquid changes its composition and surface tension by evaporation.
Step 4)
The operation of selecting a mixed solution that can wet the surface of the test piece in 3 seconds is performed at least three times. The surface tension of the mixture thus selected is reported as the wetting tension of the film.
13)インキ密着性
フィルムの表面層(B)上に、グラビア印刷機(三谷鉄工所社製)を使用して速度50m/minでグラビア全面印刷(印刷インキ量2g/m2)を実施した。このときのインキは、水性インキ(大日本インキ化学工業社製:商品名エコファイン709白)である。
(登録商標)この印刷サンプルを用い、碁盤目剥離(2mmマス×25個、ニチバン社製セロテープ(登録商標)18mm幅使用しての、90°剥離法)により評価し(もう少し詳しく)実用性から判断して次のランク別けを行った。
碁盤目剥離部分 0個・・・・◎:印刷インキ密着性に優れる。
〃 1~5個・・・・○:印刷インキ密着性が良好。
〃 6~15個・・・・△:印刷インキ密着性に劣る。
〃 1個以上・・・・×:印刷インキ密着性がない。
13) Ink adhesion On the surface layer (B) of the film, gravure printing (printing ink amount 2 g / m 2 ) was performed at a speed of 50 m / min using a gravure printing machine (manufactured by Mitani Iron Works Co., Ltd.). The ink at this time is a water-based ink (manufactured by Dainippon Ink & Chemicals, Inc .: trade name Eco Fine 709 White).
(Registered trademark) Using this print sample, it was evaluated by grid peeling (2 mm square x 25 pieces, 90 ° peeling method using cello tape (registered trademark) 18 mm width manufactured by Nichiban Co., Ltd.). Judgment was made and the next ranking was performed.
Cross-section peeling part: 0 ·····: Excellent in printing ink adhesion.
〃 1 to 5 ... ○: Good adhesion of printing ink.
6 6 to 15 ・ ・ ・ Δ: Poor adhesion to printing ink.
〃 1 or more ········ ×: No printing ink adhesion.
14)ラミネート強度
ラミネート強度は以下のような手順により測定した。
手順1)シーラントフィルムとのラミネートフィルムの作成
連続式のドライラミネート機を用いて以下の様に行った。
実施例、比較例で得られた二軸配向ポリプロピレン系フィルムの表面層(B)面に接着剤を乾燥時塗布量が3.0g/m2となるようにグラビアコートした後、乾燥ゾーンに導き80℃、5秒で乾燥した。引き続き下流側に設けられたロール間でシーラントフィルムと貼り合わせた(ロール圧力0.2MP、ロール温度:60℃)。得られたラミネートフィルムは巻き取った状態で40℃、3日間のエージング処理を行った。
なお、接着剤は主剤(東洋モートン社製、TM329)17.9質量%、硬化剤(東洋モートン社製、CAT8B)17.9質量%および酢酸エチル64.2質量%を混合して得られたエーテル系接着剤を使用し、シーラントフィルムは東洋紡社製無延伸ポリプロピレン系フィルム(パイレン(登録商標)CT P1128、厚み30μm)を使用した。
手順2)ラミネート強度の測定
上記で得られたラミネートフィルムを二軸配向ポリプロピレン系フィルムの縦方向に長辺を持つ短冊状(長さ200mm、幅15mm)に切り出し、引張試験機(テンシロン、オリエンテック社製)を用いて、23℃の環境下200mm/分の引張速度でT字剥離した際の剥離強度(N/15mm)を測定した。測定は3回行い、その平均値をラミネート強度とした。
14) Laminate strength The laminate strength was measured by the following procedure.
Procedure 1) Preparation of a laminate film with a sealant film A continuous dry laminating machine was used as follows.
The surface layer (B) surface of the biaxially oriented polypropylene film obtained in Examples and Comparative Examples was gravure-coated so that the coating amount when dried was 3.0 g / m 2, and then led to the drying zone. Dried at 80 ° C. for 5 seconds. Subsequently, it was bonded to a sealant film between rolls provided on the downstream side (roll pressure 0.2 MP, roll temperature: 60 ° C.). The obtained laminate film was subjected to an aging treatment at 40 ° C. for 3 days while being wound up.
The adhesive was obtained by mixing 17.9% by mass of a main agent (manufactured by Toyo Morton, TM329), 17.9% by mass of a curing agent (CAT8B, manufactured by Toyo Morton) and 64.2% by mass of ethyl acetate. An ether adhesive was used, and a non-stretched polypropylene film (Pyrene (registered trademark) CTP1128, thickness 30 μm) manufactured by Toyobo Co., Ltd. was used as the sealant film.
Procedure 2) Measurement of laminate strength The laminate film obtained above was cut into a strip shape (length: 200 mm, width: 15 mm) having a long side in the longitudinal direction of a biaxially oriented polypropylene film, and a tensile tester (Tensilon, Orientec) Was used, and the peel strength (N / 15 mm) at the time of T-peeling at a tensile rate of 200 mm / min in an environment of 23 ° C. was measured. The measurement was performed three times, and the average value was taken as the laminate strength.
(原料樹脂)
下記実施例、比較例で使用したポリプロピレン系樹脂原料の詳細を表1に示す。
(Raw resin)
The details of the polypropylene resin materials used in the following examples and comparative examples are shown in Table 1.
(実施例1)
基材層(A)には、表1に示すポリプロピレン単独重合体PP-1を用いた。
また、表面層(B)には、表1に示すポリプロピレン単独重合体PP-1が49重量%と表1に示すエチレン共重合ポリプロピレン重合体PP-3が51重量部の割合で混合された組成物に、市販のポリメチルメタクリレート(PMMA)粒子(平均粒子径:1.4μm)をアンチブロッキング剤として、前記混合物の0.15質量%に相当する量を配合したものを使用した。このとき、ポリプロピレン単独重合体PP-1が49重量%部とエチレン共重合ポリプロピレン重合体PP-3が51重量%の混合物のメルトフローレート(g/10分)は5.3であった。
基材層(A)は60mm押出機、表面層(B)は65mm押出機を用いて、それぞれ原料樹脂を250℃で溶融し、Tダイからシート状に2層に共押し出しし、基材層(A)側が冷却ロールに接するようにして、30℃の冷却ロールで冷却固化した後、125℃縦方向(MD)に4.5倍に延伸した。次いでテンター内で、フィルム幅方向両端をクリップで挟み、170℃で予熱後、158℃で幅方向(TD)に8.2倍に延伸し、幅方向(TD)に6.7%緩和させながら、165℃で熱固定した。
このときの製膜条件を製膜条件aとした。
こうして、基材層(A)と表面層(B)が1層ずつ積層された二軸配向ポリプロピレン系フィルムを得た。
二軸配向ポリプロピレン系フィルムの表面層(B)側にソフタル・コロナ・アンド・プラズマGmbH社製のコロナ処理機を用いて、印加電流値:0.75Aの条件で、コロナ処理を施した後、ワインダーで巻き取った。得られたフィルムの厚みは20μmであった。
Example 1
Polypropylene homopolymer PP-1 shown in Table 1 was used for the base material layer (A).
In the surface layer (B), 49% by weight of the polypropylene homopolymer PP-1 shown in Table 1 and 51 parts by weight of the ethylene copolymer polypropylene polymer PP-3 shown in Table 1 were mixed. What mixed the quantity corresponding to 0.15 mass% of the said mixture was used for the thing by using commercially available polymethylmethacrylate (PMMA) particle | grains (average particle diameter: 1.4 micrometers) as an antiblocking agent. At this time, the melt flow rate (g / 10 min) of a mixture of 49% by weight of the polypropylene homopolymer PP-1 and 51% by weight of the ethylene copolymer polypropylene polymer PP-3 was 5.3.
The base material layer (A) was melted at 250 ° C. using a 60 mm extruder and the surface layer (B) was a 65 mm extruder, respectively, and coextruded into two layers in a sheet form from a T die. After the (A) side was in contact with the cooling roll and cooled and solidified with a 30 ° C. cooling roll, it was stretched 4.5 times in the longitudinal direction (MD) of 125 ° C. Next, in the tenter, the film width direction both ends are clipped, preheated at 170 ° C., stretched 8.2 times in the width direction (TD) at 158 ° C., and relaxed by 6.7% in the width direction (TD). And heat-fixed at 165 ° C.
The film forming condition at this time was defined as film forming condition a.
Thus, a biaxially oriented polypropylene film in which the base material layer (A) and the surface layer (B) were laminated one by one was obtained.
After the corona treatment was performed on the surface layer (B) side of the biaxially oriented polypropylene film using a corona treatment machine manufactured by Sophtal Corona & Plasma GmbH under the condition of applied current value: 0.75A, I wound it up with a winder. The thickness of the obtained film was 20 μm.
(実施例2)
基材層(A)に使用する樹脂をポリプロピレン樹脂PP-2に変更し、基材層(A)は60mm押出機、表面層(B)は65mm押出機を用いて、それぞれ原料樹脂を250℃で溶融し、Tダイからシート状に共押し出しし、30℃の冷却ロールで冷却固化した後、135℃縦方向(MD)に4.5倍に延伸した。次いでテンター内で、フィルム幅方向両端をクリップで挟み、175℃で予熱後、160℃で幅方向(TD)に8.2倍に延伸し、幅方向(TD)に6.7%緩和させながら、170℃で熱固定した。このときの製膜条件を製膜条件bとした。
こうして、基材層(A)と表面層(B)が1層ずつ積層された二軸配向ポリプロピレン系フィルムを得た。
(Example 2)
The resin used for the base material layer (A) is changed to polypropylene resin PP-2, the base material layer (A) is a 60 mm extruder and the surface layer (B) is a 65 mm extruder, and the raw material resin is 250 ° C. respectively. And then coextruded into a sheet form from a T-die, cooled and solidified with a 30 ° C. cooling roll, and then stretched 4.5 times in the 135 ° C. longitudinal direction (MD). Next, in the tenter, both ends in the film width direction are sandwiched between clips, preheated at 175 ° C., stretched 8.2 times in the width direction (TD) at 160 ° C., and relaxed by 6.7% in the width direction (TD). And heat-fixed at 170 ° C. The film forming conditions at this time were set as film forming conditions b.
Thus, a biaxially oriented polypropylene film in which the base material layer (A) and the surface layer (B) were laminated one by one was obtained.
(実施例3)
基材層(A)の厚みを38μmに変更した以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。
(Example 3)
A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that the thickness of the base material layer (A) was changed to 38 μm.
(実施例4)
基材層(A)の厚みを18μmに変更した以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。
Example 4
A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that the thickness of the base material layer (A) was changed to 18 μm.
(比較例1)
表面層(B)には、ポリプロピレン単独重合体PP-1に対して、アンチブロッキング剤として、ポリメチルメタクリレート(PMMA)粒子(平均粒子径:1.4μm)を0.15質量%配合したものを使用した以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。
(Comparative Example 1)
In the surface layer (B), 0.15% by mass of polymethyl methacrylate (PMMA) particles (average particle size: 1.4 μm) as an antiblocking agent is blended with the polypropylene homopolymer PP-1. A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that it was used.
(比較例2)
表面層(B)には、ポリプロピレン単独重合体PP-1とPP-4を使用した以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。
(Comparative Example 2)
A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that polypropylene homopolymers PP-1 and PP-4 were used for the surface layer (B).
(比較例3)
表面層(B)には、アンチブロッキング剤を使用しないこと以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。
(Comparative Example 3)
For the surface layer (B), a biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that no antiblocking agent was used.
(比較例4)
基材層(A)には、ポリプロピレン単独重合体PP-1に、帯電防止剤として、ステアリルジエタノールアミンステアレート(松本油脂(株) KYM-4K)をポリプロピレン単独重合体PP-1に対して1.0質量%配合したものを使用した以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。得られたフィルムの物性は、表3に示すとおりである。
(Comparative Example 4)
For the base material layer (A), polypropylene homopolymer PP-1 and stearyl diethanolamine stearate (MATMOTO KYM-4K) as an antistatic agent were added to the polypropylene homopolymer PP-1. A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that 0% by mass was used. Table 3 shows the physical properties of the obtained film.
(比較例5)
二軸配向ポリプロピレン系フィルムの表面層(B)側にコロナ処理を施さない以外は、実施例1と同様にして二軸延伸積層ポリプロピレン系フィルムを得た。
(Comparative Example 5)
A biaxially stretched laminated polypropylene film was obtained in the same manner as in Example 1 except that the surface layer (B) side of the biaxially oriented polypropylene film was not subjected to corona treatment.
(比較例6)
40℃の冷却ロールで冷却固化した後、135℃縦方向(MD)に4.5倍に延伸し、次いでテンター内で、フィルム幅方向両端をクリップで挟み、175℃で予熱後、163℃で幅方向(TD)に8.2倍に延伸し、幅方向(TD)に6.7%緩和させながら、1772℃で熱固定し、コロナ処理を施さない以外は、実施例1と同様に行った。
このときの製膜条件を製膜条件cとした。
(Comparative Example 6)
After cooling and solidifying with a 40 ° C. cooling roll, the film was stretched 4.5 times in the longitudinal direction (MD) at 135 ° C., and then sandwiched with clips at both ends in the film width direction in a tenter, preheated at 175 ° C. and then at 163 ° C. Except that the film was stretched 8.2 times in the width direction (TD) and relaxed by 6.7% in the width direction (TD), heat fixed at 1772 ° C., and subjected to the same corona treatment, but the same as in Example 1. It was.
The film forming condition at this time was defined as film forming condition c.
上記実施例、比較例で使用した原料、製膜条件、及び得られたフィルムの物性を、それぞれ表2、表3、表4に示す。 Table 2, Table 3, and Table 4 show the raw materials used in the above Examples and Comparative Examples, the film forming conditions, and the physical properties of the obtained films, respectively.
実施例1~4で得られた二軸延伸積層ポリプロピレン系フィルムは、ラミネート強度が高く、印刷インキ密着性に優れるものであった。さらに熱収縮率が低く、ヤング率は高かった。
それに対して、比較例1~5のフィルムは、いずれも印刷インキ密着性に劣るものであった。
また、比較例6のフィルムは、いずれもヘイズが高く、透明性に劣るものであった。
The biaxially stretched laminated polypropylene films obtained in Examples 1 to 4 had high laminate strength and excellent printing ink adhesion. Furthermore, the thermal shrinkage rate was low and the Young's modulus was high.
On the other hand, the films of Comparative Examples 1 to 5 were all poor in printing ink adhesion.
Moreover, all the films of Comparative Example 6 had high haze and were inferior in transparency.
本発明の二軸延伸積層ポリプロピレン系フィルムは、印刷インキ密着性良好であるため、菓子などに使用される食品包装用はもちろんのこと、ラベル等にも使用可能であり、また、安価にフィルムを製造できるため、産業上有用である。 Since the biaxially stretched laminated polypropylene film of the present invention has good printing ink adhesion, it can be used not only for food packaging used for confectionery, but also for labels, etc. Since it can be manufactured, it is industrially useful.
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| KR1020197022935A KR102500332B1 (en) | 2017-02-01 | 2018-01-22 | Biaxially oriented polypropylene-based film |
| JP2021203409A JP7689488B2 (en) | 2017-02-01 | 2021-12-15 | Method for producing biaxially oriented polypropylene film |
| JP2023001551A JP7548346B2 (en) | 2017-02-01 | 2023-01-10 | Method for producing biaxially oriented polypropylene film |
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| KR102835409B1 (en) | 2023-06-08 | 2025-07-18 | 에쓰대시오일 주식회사 | Polypropylene resin composition and preparation method thereof |
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| JP7614570B2 (en) | 2021-01-12 | 2025-01-16 | 東洋紡株式会社 | Laminated Film |
| JPWO2022153906A1 (en) * | 2021-01-12 | 2022-07-21 | ||
| JP2024008949A (en) * | 2021-01-12 | 2024-01-19 | 東洋紡株式会社 | laminated film |
| JP7708187B2 (en) | 2021-07-16 | 2025-07-15 | 東洋紡株式会社 | Biaxially oriented laminated polypropylene film |
| JPWO2023286541A1 (en) * | 2021-07-16 | 2023-01-19 | ||
| WO2023127534A1 (en) | 2021-12-28 | 2023-07-06 | 東洋紡株式会社 | Biaxially-oriented polypropylene film |
| KR20240130086A (en) | 2021-12-28 | 2024-08-28 | 도요보 가부시키가이샤 | Biaxially oriented polypropylene film |
| KR20240126040A (en) | 2021-12-28 | 2024-08-20 | 도요보 가부시키가이샤 | Biaxially oriented polypropylene film |
| JP7509328B2 (en) | 2021-12-28 | 2024-07-02 | 東洋紡株式会社 | Biaxially oriented polypropylene film |
| WO2023127535A1 (en) | 2021-12-28 | 2023-07-06 | 東洋紡株式会社 | Biaxially oriented polypropylene-based film |
| JPWO2023127535A1 (en) * | 2021-12-28 | 2023-07-06 | ||
| WO2023234417A1 (en) * | 2022-06-02 | 2023-12-07 | 東洋紡株式会社 | Mold release film |
Also Published As
| Publication number | Publication date |
|---|---|
| KR102500332B1 (en) | 2023-02-14 |
| JPWO2018142983A1 (en) | 2019-11-21 |
| KR20190111975A (en) | 2019-10-02 |
| JP7689414B2 (en) | 2025-06-06 |
| JP2022033172A (en) | 2022-02-28 |
| JP7689488B2 (en) | 2025-06-06 |
| JP7548346B2 (en) | 2024-09-10 |
| JP2023038239A (en) | 2023-03-16 |
| TWI793097B (en) | 2023-02-21 |
| TW201834861A (en) | 2018-10-01 |
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