JP7164053B2 - biaxially oriented polypropylene film - Google Patents

Description

The present invention relates to a biaxially oriented polypropylene film having excellent rigidity and heat resistance. More specifically, it relates to a biaxially oriented polypropylene film that can be suitably used as a packaging bag because it easily retains the bag shape when used as a packaging bag and causes less wrinkles in the sealed portion when heat-sealed.

Biaxially oriented polypropylene films are used for packaging and industrial applications because they are moisture-proof and have necessary rigidity and heat resistance. In recent years, in consideration of the environment, it is required to maintain the strength even if the volume is reduced (thickness of the film is reduced), and for that purpose, it is essential to significantly improve the rigidity. As a means to improve rigidity, the crystallinity and melting point of the polypropylene resin are improved by improving the catalyst and process technology during the polymerization of polypropylene resin, and the degree of orientation of the film is improved by increasing the draw ratio during the film production process. There was a technology to increase However, there is a problem that heat resistance is lowered at the same time as rigidity is increased, and there has been no biaxially oriented polypropylene film having sufficient rigidity and heat resistance. In addition, if the rigidity is improved and the volume of the film is reduced, the water vapor barrier property is lowered, and the moisture resistance is impaired, so there is a problem that the food deteriorates.

In the manufacturing process of a biaxially oriented polypropylene film, after stretching in the width direction, the first heat treatment is performed while the film is relaxed at a temperature below the temperature during the width direction stretching, and in the second step, the heat treatment is performed at the temperature between the first step and the width direction stretching temperature. (see, for example, Patent Document 1, etc.) and a method of further stretching in the longitudinal direction after stretching in the width direction (see, for example, Patent Documents 2 and 3, etc.) have been proposed.
However, although the film described in Patent Literature 2 is excellent in rigidity, wrinkles are likely to occur in the sealed portion after heat sealing, and the film is inferior in heat resistance. In addition, the orientation of the film described in Patent Document 1 is low and the rigidity is not sufficient. The film described in Patent Document 3 is sequentially biaxially stretched, and the film oriented in the width direction is re-stretched in the longitudinal direction, so the molecular chains are not sufficiently aligned in the longitudinal direction, and the rigidity in the longitudinal direction is low. It was something. In addition, since relaxation is performed in the width direction, the orientation in the width direction is low and the rigidity is not sufficient.

WO2016/182003 international publication JP 2013-177645 A Japanese Patent Application Laid-Open No. 2001-40111

An object of the present invention is to solve the problems described above. That is, it relates to a biaxially oriented polypropylene film that achieves both film rigidity and heat resistance at temperatures as high as 150°C. Specifically, it has high rigidity and can easily maintain its shape when used as a packaging bag even when the film is thinned. Another object of the present invention is to provide a biaxially oriented polypropylene film which, when heat-sealed, causes less wrinkles in the sealed portion and its surroundings.

As a result of intensive studies conducted by the present inventors in order to achieve these objects, a biaxially oriented polypropylene film satisfying the following (1), (2) and (3).
(1) Thermal shrinkage at 150° C. is 10% or less in the longitudinal direction and 30% or less in the width direction.
(2) The stress at 5% elongation in the width direction at 23°C is 140 MPa or more.
(3) Heat shrinkage in width direction at 150°C (%) and stress at 5% elongation in width direction at 23°C (MPa)
satisfies the following equation.
Stress at 5% elongation in the width direction at 23 ° C. (MPa) ≥ Heat shrinkage rate in the width direction at 150 ° C. (%) × 4.0 + 140

In this case, the biaxially oriented polypropylene film preferably satisfies (4) and (5) below.
(4) The heat shrinkage rate at 120°C is 2.0% or less in the longitudinal direction and 10.0% or less in the width direction.
(5) The thermal contraction rate (%) in the width direction at 120°C and the tensile modulus (GPa) in the width direction at 23°C satisfy the following formulas.
Tensile elastic modulus in the width direction at 23°C (GPa) ≥ Heat shrinkage rate in the width direction at 120°C (%) x 0.1 + 7.0

In this case, it is preferable that the longitudinal refractive index Ny of the biaxially oriented polypropylene film is 1.5250 or more and ΔNy is 0.0240 or more.

In this case, in the azimuth angle dependence of the (110) plane of the polypropylene α-type crystal obtained by wide-angle X-ray diffraction measurement of the biaxially oriented film, the half width of the peak derived from the oriented crystal in the width direction is 21 ° or less.

Furthermore, in this case, it is preferable that the biaxially oriented polypropylene film has a haze of 5.0% or less.

Furthermore, in this case, it is preferable that the polypropylene resin constituting the biaxially oriented polypropylene film has a mesopentad fraction of 97.0% or more.

Furthermore, in this case, it is preferable that the polypropylene resin constituting the biaxially oriented polypropylene film has a crystallization temperature of 105° C. or higher and a melting point of 161° C. or higher.

Furthermore, in this case, it is preferable that the polypropylene resin constituting the biaxially oriented polypropylene film has a melt flow rate of 4.0 g/10 minutes or more.

Furthermore, in this case, it is preferable that the amount of components having a molecular weight of 100,000 or less in the polypropylene resin constituting the biaxially oriented polypropylene film is 35% by mass or more.

Furthermore, in this case, it is preferable that the degree of orientation of the biaxially oriented polypropylene film is 0.85 or more.

The biaxially oriented polypropylene film of the present invention has high rigidity and can be thinned, and at the same time, can maintain gas barrier properties equivalent to the thickness of the conventional film even when the film is thinned. It is a biaxially oriented polypropylene film with few wrinkles in and around the seal area. Therefore, it can be suitably used for packaging, industrial use, and the like.

The biaxially oriented polypropylene film of the present invention will be described in more detail below.
The biaxially oriented polypropylene film of the present invention comprises a polypropylene resin composition containing a polypropylene resin as a main component. The "main component" means that the proportion of the polypropylene resin in the polypropylene resin composition is 90% by mass or more, more preferably 93% by mass or more, more preferably 95% by mass or more, and particularly preferably is 97% by mass or more.

(polypropylene resin)
The polypropylene resin used in the present invention may be a polypropylene homopolymer or a copolymer with ethylene and/or an α-olefin having 4 or more carbon atoms. A propylene homopolymer substantially free of ethylene and/or an α-olefin having 4 or more carbon atoms is preferred, and even if it contains ethylene and/or an α-olefin component having 4 or more carbon atoms, ethylene and/or The amount of α-olefin components having 4 or more carbon atoms is preferably 1 mol % or less, more preferably 0.5 mol % or less, still more preferably 0.3 mol % or less, and particularly preferably 0.3 mol % or less. It is 1 mol or less. Within the above range, the crystallinity tends to be improved. Examples of α-olefin components having 4 or more carbon atoms constituting such a copolymer include 1-butene, 1-pentene, 3-methylpentene-1, 3-methylbutene-1, 1-hexene, 4-methyl Pentene-1,5-ethylhexene-1,1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-heptadecene, 1-octadecene, 1-eicosene and the like.
As the polypropylene resin, two or more different polypropylene homopolymers, copolymers with ethylene and/or α-olefins having 4 or more carbon atoms, and mixtures thereof can be used.

(Steric regularity)
The mesopentad fraction ([mmmm]%), which is an index of stereoregularity of the polypropylene resin used in the present invention, is preferably in the range of 97.0 to 99.9%, more preferably 97.5 to 99.7. %, more preferably 98.0 to 99.5%, and particularly preferably 98.5 to 99.3%.
When it is 97.0% or more, the crystallinity of the polypropylene resin is enhanced, the melting point, crystallinity, and crystal orientation of the crystals in the film are improved, and rigidity and heat resistance at high temperatures are easily obtained. When it is 99.9% or less, it is easy to reduce costs in terms of polypropylene production, and it becomes difficult to break during film formation. The mesopentad fraction is measured by a nuclear magnetic resonance method (so-called NMR method).
It is more preferably 99.5% or less. The mesopentad fraction is measured by a nuclear magnetic resonance method (so-called NMR method).
In order to make the mesopentad fraction of the polypropylene resin within the above-mentioned range, there are a method of washing the obtained polypropylene resin powder with a solvent such as n-heptane, a selection of a catalyst and / or a co-catalyst, and a polypropylene resin composition. A method of appropriately selecting components is preferably adopted.

(melting temperature)
The lower limit of the melting temperature (Tm) measured by DSC of the polypropylene resin constituting the biaxially oriented polypropylene film of the present invention is preferably 160°C, more preferably 161°C, and still more preferably 162°C. , more preferably 163°C, and even more preferably 164°C. When Tm is 160° C. or higher, rigidity and heat resistance at high temperatures are easily obtained. The upper limit of Tm is preferably 170°C, more preferably 169°C, still more preferably 168°C, still more preferably 167°C, and particularly preferably 166°C. If the Tm is 170° C. or less, it is easy to suppress cost increases in terms of polypropylene production, and it becomes difficult to break during film formation. The melting temperature can be further increased by adding a crystal nucleating agent to the polypropylene resin described above.
Tm is a sample of 1 to 10 mg packed in an aluminum pan, set in a differential scanning calorimeter (DSC), melted at 230 ° C. for 5 minutes under a nitrogen atmosphere, and scanned at a scanning speed of -10 ° C./min to 30 ° C. It is the main peak temperature of the endothermic peak associated with melting observed when the temperature is lowered, held for 5 minutes, and heated at a scanning rate of 10° C./min.

(crystallization temperature)
The lower limit of the crystallization temperature (Tc) measured by DSC of the polypropylene resin constituting the biaxially oriented polypropylene film of the present invention is 105°C, preferably 108°C, more preferably 110°C. When Tc is 105° C. or more, crystallization is likely to proceed in the width direction stretching and the subsequent cooling step, and rigidity and heat resistance at high temperatures are likely to be obtained. The upper limit of Tc is preferably 135°C, more preferably 133°C, still more preferably 132°C, even more preferably 130°C, particularly preferably 128°C, and most preferably 127°C. is. When Tc is 135° C. or less, it is difficult to increase the cost of polypropylene production, and it is difficult to break during film formation. The crystallization temperature can be further increased by adding a crystal nucleating agent to the polypropylene resin described above.
Tc is observed when a sample of 1 to 10 mg is packed in an aluminum pan and set in a DSC, melted at 230 ° C. for 5 minutes under a nitrogen atmosphere, and cooled to 30 ° C. at a scanning speed of -10 ° C./min. is the main peak temperature of the exothermic peak

(melt flow rate)
The melt flow rate (MFR) of the polypropylene resin constituting the biaxially oriented polypropylene film of the present invention is 4 when measured according to Condition M (230°C, 2.16 kgf) of JIS K 7210 (1995). It is preferably 0 g/10 min or more and 30 g/10 min or less, more preferably 4.5 g/10 min or more and 25 g/10 min or less, and 4.8 g/10 min or more and 22 g/10 min or less. It is more preferably 5.0 g/10 min or more and 20 g/10 min or less, and most preferably 6.0 g/10 min or more and 20 g/10 min or less.
When the melt flow rate (MFR) of the polypropylene resin is 4.0 g/10 minutes or more, it is easy to obtain a biaxially oriented polypropylene film with low thermal shrinkage.
Moreover, when the melt flow rate (MFR) of the polypropylene resin is 30 g/10 minutes or less, the film formability of the film is easily maintained.

From the viewpoint of film properties, the lower limit of the melt flow rate (MFR) (230 ° C., 2.16 kgf) of the polypropylene resin constituting the film is preferably 5.0 g / 10 minutes, more preferably 5.5 g / 10 minutes, It is more preferably 6.0 g/10 minutes, particularly preferably 6.3 g/10 minutes, and most preferably 6.5 g/10 minutes.
When the melt flow rate (MFR) of the polypropylene resin is 5.0 g/10 minutes or more, the amount of low-molecular weight components of the polypropylene resin constituting the film increases, so the width direction stretching step in the film forming step described later is performed. By adopting it, in addition to further promoting the oriented crystallization of the polypropylene resin and making it easier to increase the degree of crystallinity in the film, the entanglement between the polypropylene molecular chains in the amorphous part is reduced, and the heat resistance is improved. It is easy to increase sexuality.
In order to keep the melt flow rate (MFR) of the polypropylene resin within the above range, it is preferable to adopt a method of controlling the average molecular weight and molecular weight distribution of the polypropylene resin.

That is, the lower limit of the amount of components having a molecular weight of 100,000 or less in the GPC integrated curve of the polypropylene resin constituting the film of the present invention is 35% by mass, preferably 38% by mass, more preferably 40% by mass, More preferably 41% by mass, particularly preferably 42% by mass.
The upper limit of the amount of components having a molecular weight of 100,000 or less in the GPC integrated curve is preferably 65% by mass, more preferably 60% by mass, and still more preferably 58% by mass. When the amount of components having a molecular weight of 100,000 or less in the GPC integrated curve is 65% by mass or less, the film strength is less likely to decrease.
At this time, if a high-molecular-weight component with a long relaxation time or a long-chain branched component is included, the amount of the component with a molecular weight of 100,000 or less contained in the polypropylene resin can be easily adjusted without significantly changing the overall viscosity, thereby improving the rigidity. It is easy to improve the film formability without significantly affecting the heat shrinkage and heat shrinkage.

(Molecular weight distribution)
In the polypropylene resin used in the present invention, the lower limit of the weight average molecular weight (Mw) / number average molecular weight (Mn), which is an index of the breadth of the molecular weight distribution, is preferably 3.5, more preferably 4, and further 4.5 is preferred, and 5 is particularly preferred. The upper limit of Mw/Mn is preferably 30, more preferably 25, even more preferably 23, particularly preferably 21, and most preferably 20.
Mw/Mn can be obtained using gel permeation chromatography (GPC). When Mw/Mn is within the above range, it is easy to increase the amount of components having a molecular weight of 100,000 or less.

The molecular weight distribution of polypropylene resin can be determined by polymerizing components with different molecular weights in multiple stages in a series of plants, by blending components with different molecular weights offline using a kneader, or by blending catalysts with different performance. or by using a catalyst capable of realizing a desired molecular weight distribution. The shape of the molecular weight distribution obtained by GPC has a single peak in a GPC chart with the logarithm (logM) of the molecular weight (M) on the horizontal axis and the differential distribution value (weight fraction per logM) on the vertical axis. It may have a smooth molecular weight distribution, or may have a molecular weight distribution with multiple peaks or shoulders.

(Method for forming biaxially oriented polypropylene film)
The biaxially oriented polypropylene film of the present invention is preferably obtained by preparing an unstretched sheet made of the polypropylene resin composition containing the polypropylene resin as a main component, and biaxially stretching the sheet. As the biaxial stretching method, it can be obtained by any of the inflation simultaneous biaxial stretching method, the tenter simultaneous biaxial stretching method, and the tenter sequential biaxial stretching method. It is preferable to employ an axial stretching method. In particular, it is preferable to stretch in the width direction after stretching in the longitudinal direction, but it is also possible to stretch in the longitudinal direction after stretching in the width direction.

Next, the method for producing the biaxially oriented polypropylene film of the present invention will be described below, but the method is not necessarily limited to this. In addition, the biaxially oriented polypropylene film of the present invention may be laminated with a layer having other functions on at least one side thereof. Lamination may be performed on one side or both sides. In such a case, the above-mentioned polypropylene resin composition may be used as the resin composition for the other layer and the center layer. Also, it may be different from the polypropylene resin composition described above. The number of layers to be laminated may be 1 layer, 2 layers, or 3 layers or more per side, but 1 layer or 2 layers are preferable from the viewpoint of manufacturing. As a lamination method, for example, co-extrusion by a feed block system or a multi-manifold system is preferable. In particular, for the purpose of improving the workability of the biaxially oriented polypropylene film, a heat-sealable resin layer can be laminated within a range in which the properties are not deteriorated. In addition, one side or both sides can be subjected to corona treatment for imparting printability.

In the following, an example in the case of a single layer will be described in which the tenter sequential biaxial stretching method is employed.
First, a resin composition containing a polypropylene resin is heated and melted with a single-screw or twin-screw extruder, extruded into a sheet form from a T-die, grounded on a cooling roll, and solidified by cooling. For the purpose of promoting the solidification, it is preferable to further cool the sheet cooled by the chill roll by immersing it in a water tank or the like.

Then, the sheet is longitudinally stretched by two pairs of heated stretching rolls by increasing the number of rotations of the rear stretching rolls to obtain a uniaxially stretched film.

Subsequently, after preheating the uniaxially stretched film, it is stretched in the width direction at a specific temperature while gripping the ends of the film with a tenter type stretching machine to obtain a biaxially stretched film. This width direction stretching step will be described later in detail.

After completion of the width direction stretching step, the biaxially stretched film is heat-treated at a specific temperature to obtain a biaxially oriented film. In the heat treatment step, the film may be relaxed in the width direction.

The biaxially oriented polypropylene film thus obtained may be subjected, for example, to corona discharge treatment on at least one side, if necessary, and then wound up with a winder to obtain a film roll.

Each step will be described in detail below.
(Extrusion process)
First, a polypropylene resin composition containing polypropylene resin as the main component is heated and melted in a single-screw or twin-screw extruder at a temperature in the range of 200 ° C. to 300 ° C., and the sheet-shaped molten polypropylene resin composition coming out of the T die is extruded. , is brought into contact with a metal cooling roll to cool and solidify. The obtained unstretched sheet is preferably put into a water tank.
The temperature of the cooling roll, or the temperature of the cooling roll and the water tank, is preferably in the range of 10°C to Tc. If the transparency of the film is desired to be increased, the temperature of the cooling roll is in the range of 10 to 50°C. is preferred. When the cooling temperature is 50°C or lower, the transparency of the unstretched sheet tends to be increased, and the cooling temperature is preferably 40°C or lower, more preferably 30°C or lower. In order to increase the degree of crystal orientation after sequential biaxial stretching, it may be preferable to set the cooling temperature to 40° C. or higher, but as described above, a propylene homopolymer having a mesopentat fraction of 97.0% or higher is used. In this case, the cooling temperature is preferably 40° C. or lower for facilitating the drawing in the next step and reducing thickness unevenness, and more preferably 30° C. or lower.
The thickness of the unstretched sheet is preferably 3500 μm or less in terms of cooling efficiency, more preferably 3000 μm or less, and can be appropriately adjusted according to the thickness of the film after successive biaxial stretching. The thickness of the unstretched sheet can be controlled by the extrusion speed of the polypropylene resin composition, the lip width of the T-die, and the like.

(Longitudinal stretching process)
The lower limit of the draw ratio in the longitudinal direction is preferably 3.5 times, more preferably 3.8 times, and particularly preferably 4.2 times. Within the above range, the strength can be easily increased, and the film thickness unevenness can be reduced.
The upper limit of the draw ratio in the longitudinal direction is preferably 7.0 times, more preferably 6.0 times, and particularly preferably 7 times. Within the above range, it is easy to stretch in the width direction in the width direction stretching step, and productivity is improved.
The lower limit of the longitudinal stretching temperature is preferably Tm-30°C, more preferably Tm-27°C, still more preferably Tm-25°C. When the thickness is within the above range, subsequent width direction stretching is facilitated, and thickness unevenness is reduced. The upper limit of the longitudinal stretching temperature is preferably Tm-7°C, more preferably Tm-10°C, still more preferably Tm-12°C. Within the above range, it is easy to reduce the heat shrinkage, and it is less likely that the film will be difficult to be stretched on stretching rolls, or that the quality will be reduced due to increased surface roughness.
The longitudinal stretching may be carried out in two or more stages using three or more pairs of stretching rolls.

(Preheating process)
Before the width direction stretching step, it is necessary to heat the uniaxially stretched film after longitudinal stretching in the range of Tm to Tm+25° C. to soften the polypropylene resin composition. By making it Tm or more, softening progresses and stretching in the width direction becomes easy. By adjusting the temperature to Tm+25° C. or lower, the orientation at the time of lateral stretching proceeds, and rigidity is easily exhibited. Tm+2 to Tm+20°C is more preferable, and Tm+3 to Tm+15°C is particularly preferable. Here, the maximum temperature in the preheating step is defined as the preheating temperature.

(Width direction stretching process)
In the width direction stretching step after the preheating step, a preferable method is as follows.

In the width direction stretching step, it is preferable to stretch at a temperature of Tm-10°C or more and a preheating temperature or less. At this time, the stretching in the width direction may be started when the preheating temperature is reached, or when the temperature is lowered after reaching the preheating temperature to reach a temperature lower than the preheating temperature.
The lower limit of the temperature in the width direction stretching step is more preferably Tm-9°C, still more preferably Tm-7°C, and particularly preferably Tm-5°C. When the width direction stretching temperature is within this range, the rigidity of the obtained biaxially oriented film can be easily improved.
The upper limit of the temperature in the width direction stretching step is preferably Tm+10°C, more preferably Tm+7°C, and particularly preferably Tm+5°C. Stretching unevenness is less likely to occur when the width direction stretching temperature is within this range.
In the widthwise stretching step, a late stretching step of stretching at a lower temperature may be added subsequent to the widthwise stretching in the above temperature range.
That is, following the section (previous section) that is drawn at a temperature of Tm-10 ° C. or higher and Tm + 10 ° C. or lower, the temperature is lower than the temperature of the previous section and is drawn at a temperature of Tm-70 ° C. or higher and Tm-5 ° C. or lower. A section (late section) may be provided. By providing the early section and the late section, it is easy to increase the rigidity.
The lower limit of the stretching temperature in the latter period is preferably Tm-65°C, more preferably Tm-60°C, and even more preferably Tm-55°C. When the stretching temperature in the latter period is within this range, film formation tends to be stable.

The lower limit of the final width direction draw ratio in the width direction stretching step is preferably 9 times, more preferably 10 times. When it is 9 times or more, the rigidity tends to be increased, and the film thickness unevenness tends to be reduced. The upper limit of the width direction draw ratio is preferably 20 times, more preferably 17 times, and still more preferably 15 times. When it is 20 times or less, the heat shrinkage rate is easily reduced, and the film is less likely to break during stretching.
When adding the latter section, the total draw ratio should be within the above range. At this time, the lower limit of the draw ratio in the first drawing step is preferably 4 times, more preferably 5 times, still more preferably 6 times, and particularly preferably 6.5 times. The upper limit of the draw ratio at the end of the previous period is preferably 15 times, more preferably 14 times, and still more preferably 13 times.

It is preferable to cool the film immediately after the completion of stretching in the width direction, that is, immediately after reaching the final stretch ratio in the width direction. At this time, the cooling temperature is below the temperature for stretching in the width direction, and is preferably Tm-80 ° C. or higher and Tm-15 ° C. or lower, and Tm-80 ° C. or higher and Tm-20 ° C. or lower. more preferably Tm-80°C or higher and Tm-30°C or lower, and particularly preferably Tm-70°C or higher and Tm-35°C or lower. By adding a cooling step, crystallization occurs and the crystal orientation is fixed. After that, the orientation history is maintained even if the temperature is raised to a temperature higher than the melting point, and as a result, the crystal orientation in the film can be increased. can.
The temperature can be gradually lowered from the temperature at the end of the width direction stretching to the temperature at the time of cooling, but it can also be lowered stepwise or in one step. Lowering the temperature stepwise or in one step is preferred because it facilitates greater crystal orientation in the film.

After cooling the film, it is preferable to stretch it again in the width direction at a high temperature. The lower limit of the stretching temperature is preferably Tm-5°C, more preferably Tm, still more preferably Tm+5°C, particularly preferably Tm+7°C, and most preferably Tm+9°C. When the temperature is Tm-5°C or higher, the rigidity tends to be increased, and the heat shrinkage rate tends to decrease.
The upper limit of the stretching temperature is preferably Tm+20°C, more preferably Tm+18°C, still more preferably Tm+16°C. When the temperature is Tm+20° C. or less, the rigidity tends to be increased.
The lower limit of the re-stretching ratio at high temperature is 1.03 times, preferably 1.05 times, more preferably 1.10 times.
The upper limit of the re-stretching ratio at high temperature is preferably 2 times, more preferably 1.7 times, and still more preferably 1.5 times. If the re-stretching ratio is too large, the heat shrinkage may become too large, thickness unevenness may occur, or the film may break.

In other words, instead of immediately relaxing at a high temperature after stretching in the width direction as in the past, by stretching again in the width direction at a temperature sufficiently higher than the melting point, the heat shrinkage rate is reduced and the rigidity is further improved. I found that it is possible.
That is, it is preferable to perform stretching at Tm-5° C. or more in the process after the initial stretching in the width direction. At Tm-5°C or higher, the mobility of the molecular chains becomes sufficiently high, and the effects of entanglement of the molecular chains can be easily eliminated by stretching. crystallization proceeds sufficiently.
By cooling the film to a temperature at which the film can be crystallized after being stretched in the width direction at a high temperature, the crystal orientation is fixed, and a high-melting-point film with a high degree of crystallinity and thick crystal lamellas can be obtained.

In addition, even in portions other than the crystal lamellae, the number of molecular chains restrained by entanglement points is small, and the distortion of molecular orientation is small, so that the film is less likely to shrink even when the crystals begin to melt. Furthermore, when the degree of crystallinity is improved and the crystal lamellae are thick, the melting point tends to be high, and melting below the melting point is difficult to occur. As a result, the heat shrinkage rate tends to decrease.
As a result, it has become possible to reduce the heat shrinkage rate while further improving the rigidity.

In the normal film-forming process (extrusion - machine direction stretching - width direction stretching - heat treatment), in order to eliminate distortion due to width direction stretching performed at a temperature lower than the melting point, the film is exposed to a high temperature above the melting point in the heat treatment process, The heat shrinkage rate is lowered by applying relaxation of several percent to several tens of percent. By relaxing, it is possible to eliminate the difficulty in crystallization due to the restraint of the molecular chains, which contributes to the reduction of the thermal shrinkage rate. Conversely, however, the orientation of the molecular chains generated in the lateral stretching process in the width direction is reduced, and the rigidity is also reduced. In addition, if the temperature is too high, there is also a problem of whitening of the film.
In the normal film-forming process (extrusion - longitudinal stretching - widthwise stretching - heat treatment), by increasing the temperature in the widthwise stretching process, the mobility of the molecular chains is high, and if stretching is performed so that no strain remains, The crystal orientation is lowered because the crystals generated by the longitudinal stretching are melted.
In the method of the present invention, once the film is stretched in the width direction and sufficiently oriented in the width direction, the film having sufficient tension even if the fixed crystal orientation is melted by cooling is stretched at Tm-5 ° C. or more. Since the film is stretched again at a high temperature of 100°C, there is sufficient tension even when the film is stretched again, and there is little concern that thickness unevenness will occur or the film will break.
The draw ratio at a high temperature may be such that the entanglement of the molecular chains can be loosened and aligned, and may be 1.03 times or more. When the draw ratio is 2 times or less, thickness unevenness is less likely to occur.

Thus, by adopting the above-described longitudinal stretching step, width direction stretching step, cooling step, and high temperature stretching step, using a polypropylene resin with high stereoregularity and high melting point and high crystallinity, the polypropylene resin molecules is highly aligned in the main orientation direction (the width direction corresponds to the width direction stretching process described above), so that the crystal orientation in the resulting biaxially oriented film is strong and more crystals with a high melting point are generated. easier.

Further, by increasing the low-molecular-weight component of the polypropylene resin, the entanglement of molecular chains is further reduced, the crystallinity of the film is more likely to be increased, and the portion other than the crystal lamellae is reduced. In addition, by weakening the heat shrinkage stress in portions other than the crystal lamellae, the heat shrinkage rate tends to be further lowered.
Considering that in the prior art, if either the rigidity or the thermal shrinkage rate is improved, the other property tends to be lowered, it can be said that the present invention has an epoch-making effect.

(Heat treatment process)
The biaxially stretched film can be heat treated to further reduce heat shrinkage, if desired. The upper limit of the heat treatment temperature is preferably 183°C, more preferably 180°C, still more preferably 178°C. By setting the temperature to 183° C. or lower, the rigidity is less likely to decrease, the roughness of the film surface is not excessively increased, and the film is less likely to whiten. The lower limit of the heat treatment temperature is preferably Tm-3°C, more preferably Tm-2°C, and particularly preferably Tm.
For the purpose of adjusting the thermal shrinkage rate, the film may be relaxed (relaxed) in the width direction during the heat treatment. The upper limit of the relaxation rate is preferably 8%, more preferably 5%, and still more preferably 3 %. Within the above range, the rigidity is less likely to decrease, and film thickness fluctuations are likely to be smaller. When the rigidity is to be further increased, the heat treatment may not be performed.

(Cooling process)
After stretching in the width direction, it is preferable to cool the film immediately after stretching in the width direction again at a temperature of Tm-5° C. or higher, or immediately after the heat treatment step. The cooling temperature at this time is preferably 10° C. or higher and 140° C. or lower, more preferably 15° C. or higher and 135° C. or lower, and 20° C. or higher and 130° C. or lower. It is more preferable to set the temperature to 20° C. or more and 25° C. or less. By providing the cooling process, the state of the film can be fixed.

(film thickness)
The thickness of the biaxially oriented polypropylene film of the present invention is set according to each application, but in order to obtain the strength of the film, the lower limit of the film thickness is preferably 2 μm, more preferably 3 μm, and still more preferably 4 μm, particularly preferably 8 μm, most preferably 10 μm. When the film thickness is 2 μm or more, it is easy to obtain the rigidity of the film. The upper limit of the film thickness is preferably 100 μm, more preferably 80 μm, even more preferably 60 μm, particularly preferably 50 μm, most preferably 40 μm. When the film thickness is 100 µm or less, the cooling rate of the unstretched sheet during the extrusion process is difficult to decrease.
The biaxially oriented polypropylene film of the present invention is usually produced as a roll having a width of about 2000 to 12000 mm and a length of about 1000 to 50000 m, and wound into a film roll. Furthermore, it is slit according to each application and provided as a slit roll having a width of 300 to 2000 mm and a length of about 500 to 5000 m. The biaxially oriented polypropylene film of the present invention makes it possible to obtain longer film rolls.

(Thickness uniformity)
The lower limit of the thickness uniformity of the biaxially oriented polypropylene film of the present invention is preferably 0%, more preferably 0.1%, still more preferably 0.5%, and particularly preferably 1%. The upper limit of thickness uniformity is preferably 20%, more preferably 17%, still more preferably 15%, particularly preferably 12%, and most preferably 10%. Within the above range, defects are unlikely to occur during post-processing such as coating and printing, and it is easy to use for applications requiring precision.
The measurement method was as follows. A test piece of 40 mm in the width direction is cut out from the constant region where the film properties are stable in the length direction of the film, and a film feeding device manufactured by Micron Keiseki Co., Ltd. (manufacturing number: A90172 is used) and a film manufactured by Anritsu Co., Ltd. Using a thickness continuous measuring device (product name: K-313A wide-range high-sensitivity electronic micrometer), the film thickness was continuously measured over 20000 mm, and the thickness uniformity was calculated from the following formula.
Thickness uniformity (%) = [(maximum thickness - minimum thickness) / average thickness] x 100

(Film properties)
The biaxially oriented polypropylene film of the present invention is characterized by the following properties. Here, the “longitudinal direction” in the biaxially oriented polypropylene film of the present invention is the direction corresponding to the flow direction in the film manufacturing process, and the “width direction” is the direction perpendicular to the flow direction in the film manufacturing process. is. For a polypropylene film in which the flow direction in the film manufacturing process is unknown, a wide-angle X-ray is incident in the direction perpendicular to the film surface, and the scattering peak derived from the (110) plane of the α-type crystal is scanned in the circumferential direction, The direction in which the obtained diffraction intensity distribution has the highest diffraction intensity is defined as the "longitudinal direction", and the direction orthogonal thereto is defined as the "width direction".

The heat shrinkage (%) in the width direction at 150°C and the stress (MPa) at 23°C at 5% elongation in the width direction of the biaxially oriented polypropylene film of the present invention satisfy the following formulae.
By satisfying the following formula, the rigidity is higher and the heat shrinkage rate at high temperatures is smaller, so when it is used as a packaging bag, it is easier to maintain the shape of the bag, and it can be heat-sealed at high temperatures. The deformation of the film during processing is less likely to occur, and the packaging quality is further improved. In addition, it becomes possible to make the film thinner, which contributes to the volume reduction of the packaging material.
Stress at 5% elongation in the width direction at 23 ° C. (MPa) ≥ Heat shrinkage rate in the width direction at 150 ° C. (%) × 4.0 + 140
In addition, it is preferable that the heat shrinkage (%) in the width direction at 150°C and the stress (MPa) at 5% elongation in the width direction at 23°C of the biaxially oriented polypropylene film of the present invention satisfy the following formulae.
Stress at 5% elongation in the width direction at 23 ° C. (MPa) ≥ Heat shrinkage rate in the width direction at 150 ° C. (%) × 4.0 + 150
Furthermore, the heat shrinkage (%) in the width direction at 150 ° C. and the stress (MPa) at 5% elongation in the width direction at 23 ° C. of the biaxially oriented polypropylene film of the present invention more preferably satisfy the following formula. .
Stress at 5% elongation in the width direction at 23 ° C. (MPa) ≥ Heat shrinkage rate in the width direction at 150 ° C. (%) × 4.0 + 160

(150°C heat shrinkage rate)
The upper limit of the longitudinal heat shrinkage at 150°C of the biaxially oriented polypropylene film of the present invention is 10%, preferably 7.0%, more preferably 6.0%, and even more preferably 5.0%, particularly preferably 4.0% or less. The upper limit of the heat shrinkage rate in the width direction at 150°C is 30%, preferably 20%, more preferably 16%, and particularly preferably 15% or less.
When the heat shrinkage in the longitudinal direction is 10% or less and the heat shrinkage in the width direction is 30% or less, wrinkles are less likely to occur during heat sealing. If the heat shrinkage ratio in the width direction at 150° C. is 0% or less and 15% or less, the distortion when the chuck portion is fused to the opening portion is preferably small. In order to reduce the heat shrinkage at 150°C, the lower limit of the amount of components having a molecular weight of 100,000 or less when measuring the gel permeation chromatography (GPC) integrated curve of the polypropylene resin constituting the film is set to 35% by mass. It is effective to

(Stress at 23°C 5% elongation)
The lower limit of F5 in the width direction at 23° C. of the biaxially oriented polypropylene film of the present invention is 140 MPa, preferably 160 MPa, more preferably 180 MPa, still more preferably 190 MPa. At 140 MPa or more, the rigidity is high, so that the bag shape when used as a packaging bag is easily maintained, and deformation of the film is less likely to occur during processing such as printing.
The upper limit of F5 in the width direction at 23°C is preferably 300 MPa, more preferably 290 MPa, and even more preferably 280 Pa. If it is 280 MPa or less, realistic manufacturing is easy, and the vertical width balance tends to be improved.
The lower limit of the stress (F5) at 5% elongation in the longitudinal direction of the biaxially oriented polypropylene film of the present invention at 23° C. is preferably 40 Pa, more preferably 42 Pa, still more preferably 46 Pa, and particularly preferably. is 48 Pa. At 40 MPa or more, the rigidity is high, so that the bag shape when made into a packaging bag is easily maintained, and deformation of the film is less likely to occur during processing such as printing.
The upper limit of F5 in the longitudinal direction at 23° C. is preferably 70 MPa, more preferably 65 MPa, still more preferably 62 MPa, particularly preferably 60 Pa. When the pressure is 70 MPa or less, realistic manufacturing becomes easy, and the vertical width balance tends to be improved.
F5 can be set within the range by adjusting the draw ratio and the relaxation ratio, or by adjusting the temperature during film formation.

The biaxially oriented polypropylene film of the present invention preferably has the following properties and structure.
(120°C heat shrinkage rate)
The upper limit of the thermal shrinkage in the longitudinal direction at 120°C of the biaxially oriented polypropylene film of the present invention is preferably 2.0%, more preferably 1.5%, and still more preferably 1.2%. , particularly preferably 1.0%. If it is 2.0% or less, it becomes difficult for printing pitch deviation to occur when printing ink is transferred. The upper limit of the heat shrinkage rate in the width direction at 120°C is 10.0% or less, preferably 5.0%, more preferably 3.5%, and particularly preferably 2.5%. When it is 10.0% or less, wrinkles are less likely to occur during heat sealing.
The heat shrinkage at 120° C. can be controlled within the range by adjusting the draw ratio, draw temperature, and heat setting temperature.

It is preferable that the thermal shrinkage rate (%) in the width direction at 120°C and the tensile modulus (GPa) in the width direction at 23°C of the biaxially oriented polypropylene film of the present invention satisfy the following formulae.
By satisfying the following formula, the rigidity is higher and the heat shrinkage rate at high temperature is smaller, so that the print pitch deviation is less likely to occur when the bag is made into a bag.
Tensile elastic modulus in the width direction at 23°C (GPa) ≥ Heat shrinkage rate in the width direction at 120°C (%) x 0.1 + 7.0
Moreover, it is more preferable that the thermal shrinkage rate (%) in the width direction at 120°C and the tensile elastic modulus (GPa) in the width direction at 23°C of the biaxially oriented polypropylene film of the present invention satisfy the following formulas.
Tensile elastic modulus in the width direction at 23°C (GPa) ≥ Heat shrinkage rate in the width direction at 120°C (%) x 0.1 + 8.0
Furthermore, it is more preferable that the biaxially oriented polypropylene film of the present invention has a widthwise thermal shrinkage rate (%) at 120°C and a widthwise tensile elastic modulus (GPa) at 23°C that satisfy the following formulas.
Tensile elastic modulus in the width direction at 23°C (GPa) ≥ Heat shrinkage rate in the width direction at 120°C (%) x 0.1 + 9.0

(23°C tensile modulus)
The lower limit of the longitudinal tensile modulus of the biaxially oriented polypropylene film of the present invention at 23° C. is preferably 2.0 GPa, more preferably 2.1 GPa, still more preferably 2.2 GPa, and particularly preferably is 2.3 GPa, most preferably 2.4 GPa, and most preferably 2.6 GPa. When the film is 2.0 GPa or more, the film has high rigidity, so that the shape of the bag can be easily maintained when used as a packaging bag, and deformation of the film is less likely to occur during processing such as printing. The upper limit of the longitudinal tensile modulus is preferably 4.0 GPa, more preferably 3.8 GPa, even more preferably 3.7 GPa, particularly preferably 3.6 GPa, and most preferably 3.6 GPa. 5 GPa. At 4.0 GPa or less, realistic production is easy, and the balance of characteristics in the longitudinal direction and the width direction tends to be improved.
The lower limit of the tensile modulus in the width direction at 23° C. of the biaxially oriented polypropylene film of the present invention is preferably 6.0 GPa, more preferably 6.5 GPa, more preferably 6.7 GPa, and still more preferably. is 7.0 GPa, particularly preferably 8.0 GPa, most preferably 8.5 GPa. When the film is 6.0 GPa or more, the rigidity is high, so that the shape of the packaging bag can be easily maintained, and deformation of the film during processing such as printing is unlikely to occur. The upper limit of the tensile modulus in the width direction is preferably 15 GPa, more preferably 13 GPa, still more preferably 12 GPa. When it is 15 GPa or less, realistic production is easy, and the balance of characteristics in the longitudinal direction and the width direction tends to be improved.
The tensile modulus can be adjusted within the range by adjusting the draw ratio and the relaxation rate, or by adjusting the temperature during film formation.

(23°C tensile breaking strength)
The lower limit of the longitudinal tensile breaking strength at 23° C. of the biaxially oriented polypropylene film of the present invention is preferably 90 MPa, more preferably 100 MPa, even more preferably 110 MPa, and particularly preferably 115 MPa. When the pressure is 90 MPa or more, it becomes difficult for printing pitch deviation to occur when printing ink is transferred, and the durability of the packaging bag tends to be excellent. As a practical value, the upper limit of the tensile strength at break in the longitudinal direction is preferably 200 MPa, more preferably 180 MPa, and even more preferably 160 MPa. If the pressure is 200 MPa or less, the breakage of the film and the breakage of the packaging bag tend to decrease.
The lower limit of the tensile breaking strength in the width direction at 23° C. of the biaxially oriented polypropylene film of the present invention is preferably 400 MPa, more preferably 420 MPa, still more preferably 440 MPa, and particularly preferably 450 MPa. When the pressure is 400 MPa or more, printing pitch deviation is less likely to occur when printing ink is transferred, and the durability of the packaging bag tends to be excellent. As a realistic value, the upper limit of the tensile strength at break in the width direction is preferably 650 MPa, more preferably 600 MPa, and even more preferably 550 MPa. If the pressure is 650 MPa or less, the breakage of the film and the breakage of the packaging bag tend to decrease.
The tensile strength at break can be adjusted within a range by adjusting the draw ratio, draw temperature, and heat setting temperature.

(23°C tensile breaking elongation)
The lower limit of the longitudinal tensile breaking elongation at 23° C. of the biaxially oriented polypropylene film of the present invention is preferably 180%, more preferably 190%, more preferably 200%, and particularly preferably 210% or more. When it is 180% or more, the breakage of the film and the breakage of the packaging bag tend to be reduced. The upper limit of the tensile elongation at break in the longitudinal direction at 23° C. is preferably 300%, more preferably 280% as a practical value.

The lower limit of the tensile elongation at break in the width direction at 23° C. of the biaxially oriented polypropylene film of the present invention is preferably 15%, more preferably 20%, and more preferably 30%. When it is 15% or more, breakage of the film and breakage of the packaging bag tend to be reduced. The upper limit of the tensile elongation at break in the width direction at 23°C is preferably 60%, more preferably 55%, still more preferably 50%. If it is 60% or less, it becomes difficult for printing pitch deviation to occur when printing ink is transferred, and the durability of the packaging bag tends to be excellent.
The tensile elongation at break can be adjusted within a range by adjusting the draw ratio, drawing temperature, and heat setting temperature.

(refractive index)
The lower limit of the longitudinal refractive index (Nx) of the biaxially oriented polypropylene film of the present invention is preferably 1.4950, more preferably 1.4970, even more preferably 1.4980, and particularly preferably 1.4980. 1.4990, most preferably 1.5000. When it is 1.4950 or more, it is easy to increase the rigidity of the film. The upper limit of the longitudinal refractive index (Nx) is preferably 1.5100, more preferably 15070, even more preferably 1.5050. If it is 1.5100 or less, the film tends to have an excellent balance of characteristics in the longitudinal direction and the width direction.

The lower limit of the refractive index (Ny) in the width direction of the biaxially oriented polypropylene film of the present invention is preferably 1.5250, more preferably 1.5253, still more preferably 1.5255, particularly preferably 1 .5260 and most preferably 1.5265. If it is 1.5250 or more, it is easy to increase the rigidity of the film. The upper limit of the refractive index (Ny) in the width direction is preferably 1.5280, more preferably 1.5275, still more preferably 1.5270. If it is 1.5280 or less, the film tends to have an excellent balance of characteristics in the longitudinal direction and the width direction.

The lower limit of the refractive index (Nz) in the thickness direction of the biaxially oriented polypropylene film of the present invention is preferably 1.4960, more preferably 14965, still more preferably 1.4970, and particularly preferably 1.4960. 4980 and most preferably 1.4990. When it is 1.4960 or more, it is easy to increase the rigidity of the film. The upper limit of the refractive index (Nz) in the thickness direction is preferably 1.5020, more preferably 1.5015, still more preferably 1.5010. If it is 1.5020 or less, the heat resistance of the film can be easily improved.
The refractive index can be adjusted within a range by adjusting the stretching ratio, stretching temperature, and heat setting temperature.

(ΔNy)
The lower limit of ΔNy, which is the degree of orientation in the width direction of the biaxially oriented polypropylene film of the present invention, is preferably 0.0240, more preferably 0.0245, and still more preferably 0.0247. , particularly preferably 0.0250, most preferably 0.0255, particularly most preferably 0.0260. If it is 0.0240 or more, the rigidity of the film tends to be high. As a practical value, the upper limit of ΔNy is preferably 0.0280, more preferably 0.0277, still more preferably 0.0273, and particularly preferably 0.0270. If it is 0.0280 or less, thickness unevenness tends to be good. ΔNy can be set within a range by adjusting the stretching ratio, stretching temperature, and heat setting temperature of the film.
ΔNy is calculated by the following formula, where Nx, Ny, and Nz are the refractive indices along the longitudinal direction, the width direction, and the thickness direction of the film, respectively. It means the degree of orientation of the direction.
ΔNy=Ny−[(Nx+Nz)/2]

(plane orientation factor)
The lower limit of the plane orientation coefficient (ΔP) of the biaxially oriented polypropylene film of the present invention is preferably 0.0135, more preferably 0.0138, still more preferably 0.0140. When it is 0.0135 or more, the balance in the plane direction of the film is good, and the thickness unevenness is also good. As a practical value, the upper limit of the plane orientation coefficient (ΔP) is preferably 0.0155, more preferably 0.0152, and still more preferably 0.0150. If it is 0.0155 or less, it tends to be excellent in heat resistance at high temperatures. The plane orientation coefficient (ΔP) can be set within a range by adjusting the stretching ratio, stretching temperature, and heat setting temperature.
The plane orientation coefficient (ΔP) was calculated using the formula [(Nx+Ny)/2]-Nz.

(average refractive index)
The lower limit of the average refractive index of the biaxially oriented polypropylene film of the present invention is preferably 1.5080, more preferably 1.5081, still more preferably 1.5082, particularly preferably 1.5083, Most preferably it is 1.5090. As a practical value, the upper limit of the average refractive index is preferably 1.5150, more preferably 1.5140, even more preferably 1.5135, and particularly preferably 1.5130. If it is 1.5080 or more, wrinkles are less likely to occur during heat sealing of the film. The average refractive index can be adjusted within a range by adjusting the stretching ratio, stretching temperature, and heat setting temperature of the film.
The average refractive index is calculated by the following formula, where Nx, Ny, and Nz are the refractive indices along the longitudinal direction, width direction, and thickness direction of the film, respectively.
Average refractive index = (Nx + Ny + Nz)/3

(Haze)
The upper limit of the haze of the biaxially oriented polypropylene film of the present invention is preferably 5.0%, more preferably 4.5%, even more preferably 4.0%, particularly preferably 3.5%. Yes, most preferably 3.0%. When it is 5.0% or less, it is easy to use in applications where transparency is required. As a practical value, the lower limit of haze is preferably 0.1%, more preferably 0.2%, even more preferably 0.3%, and particularly preferably 0.4%. It is easy to manufacture as it is 0.1% or more. Haze is controlled by the cooling roll (CR) temperature, the width direction stretching temperature, the preheating temperature before stretching in the width direction of the tenter, the width direction stretching temperature, or the heat setting temperature, or the amount of the polypropylene resin having a molecular weight of 100,000 or less. However, the addition of an antiblocking agent or the provision of a seal layer may increase the thickness.

(Half width of diffraction peak derived from oriented crystal)
In the azimuth angle dependence of the scattering peak of the (110) plane of the polypropylene α-type crystal obtained by wide-angle X-ray measurement incident perpendicular to the film surface of the biaxially oriented polypropylene film of the present invention, the oriented crystals in the width direction of the film The upper limit of the half width (Wh) of the diffraction peak derived from is preferably 21.0°, more preferably 20.5° or less, more preferably 20.0° or less, and particularly preferably 19.0°. 5° or less, and most preferably 19.0° or less. When the half width (Wh) is 21.0° or less, it is easy to increase the rigidity of the film. In addition, it is easy to reduce the water vapor transmission rate. The lower limit of Wh is preferably 15°, more preferably 16°, still more preferably 17°.

(X-ray orientation degree)
The lower limit of the degree of X-ray orientation calculated from Wh of the biaxially oriented polypropylene film of the present invention by the following formula is preferably 0.883, more preferably 0.886, and still more preferably 0.889. . By making it 0.892 or more, it is easy to increase the rigidity.
X-ray orientation = (180-Wh)/180
The upper limit of the degree of X-ray orientation is preferably 0.917, more preferably 0.911, still more preferably 0.906. When the ratio is 0.917 or less, the film formation tends to be stable.

(Water vapor transmission rate)
The water vapor transmission rate of the biaxially oriented polypropylene film of the present invention is preferably 5.0 g/m ² ·d or less, more preferably 4.6 g/m ² ·d or less in terms of a thickness of 20 μm. , 4.3 g/m ² ·d or less. When it is 5.0 g/m ² ·d or less, sufficient water vapor barrier properties can be obtained even when the film is thinned.

(Practical properties of film)
The practical properties of the biaxially oriented polypropylene film of the present invention will be described.
(Rigidity and water vapor barrier properties)
Packaging materials used for packaging food and beverages protect the contents from various distributions, preservation such as refrigeration, and heat sterilization. A high barrier property is particularly required for the purpose of retention and content retention, and it is required that these properties are excellent even if the film is made thin.

(wrinkles during heat sealing)
In order to form a bag for packaging food, a pre-made bag is filled with contents, heated to melt and fuse the film, and sealed. Moreover, in many cases, the same process is performed when making a bag while filling food. Usually, a base film is laminated with a sealant film made of polyethylene, polypropylene, or the like, and the sealant film surfaces are fused together. As for the heating method, pressure is applied from the base film side with a heating plate to press and seal the film, and the sealing width is often about 10 mm. Since the base film is also heated at this time, the shrinkage at that time generates wrinkles. For the durability of the bag, the less wrinkles the better, and the less wrinkles the better to increase the willingness to buy. Although the sealing temperature may be about 120° C., a higher sealing temperature is required in order to increase the speed of the bag-making process, and even in that case the shrinkage is preferably small. When the zipper is to be fused to the opening of the bag, sealing at a higher temperature is required.

(Print pitch deviation)
As for the structure of the packaging film, as a basic structure, it is often composed of a laminated film of a printed base film and a sealant film. Bag making machines are used to manufacture bags, and there are three-sided bags, standing bags, gusset bags, etc., and various bag making machines are used. The print pitch deviation is considered to occur because tension and heat are applied to the film during the printing process, and the base material of the film expands and contracts. Eliminating defective products due to printing pitch deviation is important in terms of effective use of resources, and is also important in increasing purchasing motivation.

(film processing)
The biaxially oriented polypropylene film of the present invention can be printed by letterpress printing, planographic printing, intaglio printing, stencil printing, or transfer printing, depending on the application.
In addition, heat sealability is imparted by laminating unstretched sheets, monoaxially stretched films, and biaxially stretched films made of low-density polyethylene, linear low-density polyethylene, ethylene-vinyl acetate copolymer, polypropylene, and polyester as sealant films. It can also be used as a laminated body. If you want to further improve gas barrier properties and heat resistance, use unstretched sheets, uniaxially stretched films, and biaxially stretched films made of aluminum foil, polyvinylidene chloride, nylon, ethylene-vinyl alcohol copolymer, or polyvinyl alcohol as biaxially oriented polypropylene films. and the sealant film as an intermediate layer. An adhesive applied by a dry lamination method or a hot melt lamination method can be used for bonding the sealant film.
In order to improve the gas barrier property, the biaxially oriented polypropylene film, the intermediate layer film, or the sealant film can be vapor-deposited with aluminum or inorganic oxide. Vacuum vapor deposition, sputtering, and ion plating can be used as vapor deposition methods, but vacuum vapor deposition of silica, alumina, or a mixture thereof is particularly preferred.

Antifogging agents such as fatty acid esters of polyhydric alcohols, amines of higher fatty acids, amides of higher fatty acids, and ethylene oxide adducts of higher fatty acid amines and amides are used in the biaxially oriented polypropylene film of the present invention. By setting the content in the film to be in the range of 0.2 to 5% by mass, it can be made suitable for packaging perishables such as vegetables, fruits, and flowers that require a high level of freshness. can.

In addition, various additives for improving quality such as slipperiness and antistatic properties, for example, lubricants such as waxes and metal soaps for improving productivity, and plasticizers, as long as they do not impair the effects of the present invention. Agents, processing aids, heat stabilizers, antioxidants, antistatic agents, ultraviolet absorbers, and the like can also be blended.

(Industrial applicability)
Since the biaxially oriented polypropylene film of the present invention has the above-described excellent properties not conventionally available, it can be preferably used for packaging bags, and the thickness of the film can be made thinner than before.

Furthermore, rigidity is required for applications that are used at high temperatures, such as insulation films for capacitors and motors, back sheets for solar cells, barrier films of inorganic oxides, base films for transparent conductive films such as ITO, and for separate films. It is also suitable for applications where In addition, it is possible to use coating agents, inks, lamination adhesives, etc., which were difficult to use in the past, and to perform coating and printing at high temperatures, which is expected to improve production efficiency.

Hereinafter, the present invention will be described in detail with reference to examples. The properties were measured and evaluated by the following methods.
(1) Melt flow rate Melt flow rate (MFR) was measured according to JISK7210 at a temperature of 230°C and a load of 2.16 kgf.

(2) Mesopentad Fraction The mesopentad fraction ([mmmm]%) of the polypropylene resin was measured using ¹³ C-NMR. The mesopentad fraction was calculated according to the method described in Zambelli et al., Macromolecules, 6:925 (1973). ¹³ C-NMR measurement was carried out at 110°C by dissolving 200 mg of a sample in a 8:2 mixture of o-dichlorobenzene and deuterated benzene at 135°C using AVANCE500 manufactured by BRUKER.

(3) Polypropylene Resin Number Average Molecular Weight, Weight Average Molecular Weight, Component Weight with Molecular Weight of 100,000 or Less, and Molecular Weight Distribution Using gel permeation chromatography (GPC), it was determined as PP equivalent molecular weight based on monodisperse polystyrene. When the baseline was not clear, the baseline was set in the range up to the lowest point of the high-molecular-weight elution peak closest to the elution peak of the standard substance.
GPC measurement conditions are as follows.
Device: HLC-8321PC/HT (manufactured by Tosoh Corporation)
Detector: RI
Solvent: 1,2,4-trichlorobenzene + dibutylhydroxytoluene (0.05%) Column: TSKgelguard column HHR (30) HT (7.5 mm ID × 7.5 cm) × 1 + TSKgelGMHHR-H (20) HT ( 7.8 mm ID x 30 cm) x 3 flow rate: 1.0 mL/min
Injection volume: 0.3 mL
Measurement temperature: 140°C
The number-average molecular weight (Mn) and mass-average molecular weight (Mw) are defined by the following equations according to the number of molecules (N _i ) at each elution position (M _i ) on the GPC curve obtained through the molecular weight calibration curve. be.
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 )
Here, the molecular weight distribution can be obtained by Mw/Mn.
Also, the ratio of components having a molecular weight of 100,000 or less was obtained from the integral curve of the molecular weight distribution obtained by GPC.

(4) Crystallization temperature (Tc), melting temperature (Tm)
Thermal measurements were performed under a nitrogen atmosphere using a Q1000 Differential Scanning Calorimeter manufactured by TA Instruments. About 5 mg was cut out from the polypropylene resin pellet and enclosed in an aluminum pan for measurement. After the temperature was raised to 230° C. and held for 5 minutes, it was cooled to 30° C. at a rate of −10° C./min, and the exothermic peak temperature was defined as the crystallization temperature (Tc). The heat of crystallization (ΔHc) was obtained by setting a baseline so that the area of the exothermic peak was smoothly connected from the start of the peak to the end of the peak. The temperature was maintained at 30° C. for 5 minutes, and the temperature was raised to 230° C. at 10° C./min, and the main endothermic peak temperature was defined as the melting temperature (Tm).

(5) Film thickness The thickness of the film was measured using a Seiko EM Millitron 1202D.

(6) Haze Measured according to JIS K7105 at 23° C. using NDH5000 manufactured by Nippon Denshoku Industries Co., Ltd.

(7) Tensile test Based on JISK7127, the tensile strength of the film in the longitudinal direction and the width direction was measured at 23°C. A sample having a size of 15 mm×200 mm was cut out from the film, and the chuck width was 100 mm, and the sample was set in a tensile tester (Instron 5965 dual-column desktop tester manufactured by Instron Japan Company Limited). A tensile test was performed at a tensile speed of 200 mm/min. From the obtained strain-stress curve, the tensile modulus was determined from the slope of the linear portion at the initial stage of elongation, and the stress at 5% elongation was determined as F5.
The tensile strength at break and the tensile elongation at break were the strength and elongation at the time when the sample broke, respectively.

(8) Thermal shrinkage rate It was measured by the following method based on JISZ1712. The film was cut into 20 mm width and 200 mm length in the longitudinal direction and width direction of the film, respectively, and hung in a hot air oven at 120° C. or 150° C. and heated for 5 minutes. The length after heating was measured, and the thermal shrinkage rate was determined as the ratio of the shrinkage length to the original length.

(9) Refractive index, ΔNy, plane orientation coefficient, average refractive index Measured at a wavelength of 589.3 nm and a temperature of 23°C using an Abbe refractometer manufactured by Atago Co., Ltd. Nx and Ny are the refractive indices along the longitudinal and width directions of the film, respectively, and Nz is the refractive index in the thickness direction. ΔNy, which is the degree of orientation in the width direction, was obtained using Nx, Ny, and Nz using the formula ΔNy=Ny−[(Nx+Nz)/2]. The plane orientation coefficient (ΔP) was calculated using the formula ΔP=[(Nx+Ny)/2]−Nz. Also, the average refractive index was calculated using (formula) average refractive index=(Nx+Ny+Nz)/3.

(10) X-ray half width and degree of orientation Measured by a transmission method using an X-ray diffractometer (SmartLab manufactured by Rigaku Co., Ltd., with αβγ attachment). X-rays with a wavelength of 1.5418 Å were used, and the X-ray output was 45 kV and 200 mA. A hybrid multidimensional pixel detector Hypix-3000 was used as a detector in 0-dimensional mode. As a slit on the incident side in the parallel beam method, Solarlit 2.5°, a length limiting slit of 10 mm, and an incident slit width of 1 mm were used. A parallel slit analyzer 0.228° was used as the slit on the light receiving side.
The camera length was 300 mm, and the integration width of the detector was 2 mm.
A sample was prepared by stacking films to a thickness of 400 μm. A detector is placed at the diffraction peak position (diffraction angle 2θ = 14.1°) of the (110) plane of the polypropylene resin α-type crystal, and the sample is rotated 360° around the thickness direction of the film to obtain the (110) plane. Azimuth dependence of diffraction intensity is obtained. The step interval was 0.5° and the measurement speed was 60°/min. From this azimuth angle dependence, the half width Wh of the diffraction peak derived from the oriented crystals in the width direction of the film was determined.
Also, using Wh, the degree of X-ray orientation was calculated from the following formula.
X-ray orientation = (180-Wh)/180

(11) Water vapor transmission rate 265 The water vapor transmission rate was measured according to JIS K7129 B method.
Using a water vapor transmission rate measuring device (PERMATRAN-W3/33, manufactured by MOCON), the water vapor transmission rate was measured in an atmosphere of 40° C. temperature and 90% RH humidity. Since the water vapor transmission rate is inversely proportional to the film thickness, the thickness of each sample to be measured was measured and converted to a value at 20 μm.

(Example 1)
As a polypropylene resin, propylene homopolymer PP-1 (Sumitomo Chemical Co., Ltd. 80 parts by weight of Sumitomo Noblen FLX80E4), MFR = 11 g/10 min, [mmmm] = 98.8%, Tc = 116.5 ° C., Tm = 161.5 ° C. Propylene homopolymer PP-2 (manufactured by Sumitomo Chemical Co., Ltd., EL80F5) was blended with 20 parts by weight.
The sheet was extruded from a T-die at 250°C, brought into contact with a cooling roll at 20°C, and put into a water bath at 20°C as it was. After that, it was stretched 4.5 times in the longitudinal direction with two pairs of rolls at 142°C, then clipped at both ends, introduced into a hot air oven, preheated at 170°C, and then 162°C as the first stage in the width direction. was stretched 10 times at . Immediately after stretching in the width direction, the film was cooled at 120° C. while being held by clips, and then re-stretched at 175° C. by 1.2 times in the width direction. Finally, it was cooled at room temperature. The thickness of the film thus obtained was 18.6 μm.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As for the physical properties, as shown in Table 3, the film was very excellent in rigidity and had a low thermal shrinkage rate at high temperatures. In addition, the film was excellent in water vapor permeability.

(Example 2)
The same procedure as in Example 1 was repeated except that the film was re-stretched at 165° C. in the width direction by 1.2 times. The thickness of the resulting film was 18.4 μm. Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As for the physical properties, as shown in Table 3, the film was very excellent in rigidity and had a low thermal shrinkage rate at high temperatures. In addition, the film was excellent in water vapor permeability.

(Example 3)
Stretched at 147 ° C. in the longitudinal direction, stretched 10 times at 165 ° C. as the first stage in the width direction, immediately after stretching in the width direction, cooled at 120 ° C. while being held by clips, and then stretched in the width direction at 177 ° C. The same procedure as in Example 1 was repeated except that the film was re-stretched by 1.2 times. The thickness of the resulting film was 18.9 µm.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As for the physical properties, as shown in Table 3, a film with high rigidity and low thermal shrinkage at high temperatures was obtained. In addition, the film was excellent in water vapor permeability.

(Example 4)
The same procedure as in Example 3 was repeated except that the film was re-stretched 1.1 times in the width direction at 177°C. The thickness of the obtained film was 20.6 μm. Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As shown in Table 3, its physical properties were high in rigidity and low in heat shrinkage at high temperatures. In addition, the film was excellent in water vapor permeability.

(Comparative example 1)
As the first step in the width direction, the film was stretched 12 times at 162°C, immediately after the film was stretched in the width direction, cooled at 100°C while being held by clips, and then heat-set at 170°C while the width was constant. As in Example 1. The thickness of the obtained film was 20.8 μm.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As shown in Table 3, its physical properties were excellent in water vapor permeability and high in rigidity, but inferior in heat shrinkage.

(Comparative example 2)
It was stretched 12 times at 162 ° C. as the first step in the width direction, and immediately after the width direction stretch, it was not cooled while being held by the clip, and was heat-set at 172 ° C. with a constant width. did the same. The thickness of the obtained film was 23.1 μm.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As for the physical properties, as shown in Table 3, the rigidity was inferior. In addition, the film was inferior in water vapor permeability.

(Comparative Example 3)
The film was stretched 12 times at 168°C as the first step in the width direction, cooled at 100°C while being held in a clip immediately after stretching in the width direction, and then heat-set at 170°C while the width was constant. As in Example 1. The thickness of the obtained film was 18.7 μm.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As for the physical properties, as shown in Table 3, the heat shrinkage rate at high temperatures was high and the rigidity was poor. In addition, the film was inferior in water vapor permeability.

(Comparative Example 4)
As a polypropylene resin, PP-3 (manufactured by Japan Polypropylene Corporation, FL203D) having MFR = 3 g / 10 minutes, [mmmm] = 94.8%, Tc = 117.2 ° C., Tm = 160.6 ° C. is used. board. The sheet was extruded from a T-die at 250°C, brought into contact with a cooling roll at 20°C, and put into a water bath at 20°C as it was. Thereafter, the film was stretched 4.5 times in the longitudinal direction at 130°C, and in the width direction stretching with a tenter, the preheating temperature was set to 168°C, and the film was stretched 8.2 times at 155°C as the first stage of stretching. Immediately after stretching in the width direction, the film was cooled at 120°C while being held by clips, and then re-stretched at 170°C in the width direction by 1.2 times. Finally, it was cooled at room temperature. The thickness of the resulting film was 18.8 μm.
Table 1 shows the structure of the polypropylene resin, and Table 2 shows the film forming conditions. As for the physical properties, as shown in Table 3, the heat shrinkage rate at high temperatures was high and the rigidity was poor. In addition, the film was inferior in water vapor permeability.

Claims (8)

A polypropylene resin composition containing 90% by mass or more of a polypropylene resin having a mesopentad fraction of 97.0% or more and 99.9% or less and a melt flow rate of 4.0 g/10 minutes or more and 30 g/10 minutes or less A biaxially oriented polypropylene film that satisfies the following (1), (2), and (3).
(1) Thermal shrinkage at 150° C. is 10% or less in the longitudinal direction and 30% or less in the width direction.
(2) The stress at 5% elongation in the width direction at 23°C is 140 MPa or more.
(3) The thermal contraction rate (%) in the width direction at 150°C and the 5% elongation stress (MPa) in the width direction at 23°C satisfy the following formulas.
Thermal contraction rate in the width direction at 150°C (%) x 4.0 + Stress at 5% elongation in the width direction at 23°C (MPa) ≥ Thermal shrinkage rate in the width direction at 150°C (%) x 4.0 0+140 The biaxially oriented polypropylene film according to claim 1, wherein the biaxially oriented polypropylene film satisfies (4) and (5) below.
(4) The heat shrinkage rate at 120°C is 2.0% or less in the longitudinal direction and 10.0% or less in the width direction.
(5) The thermal contraction rate (%) in the width direction at 120°C and the tensile modulus (GPa) in the width direction at 23°C satisfy the following formulas.
Tensile elastic modulus in the width direction at 23°C (GPa) ≥ Heat shrinkage rate in the width direction at 120°C (%) x 0.1 + 7.0 The biaxially oriented polypropylene film according to claim 1 or 2, wherein the biaxially oriented polypropylene film has a width-direction refractive index Ny of 1.5250 or more and a ΔNy of 0.0240 or more. 4. Any one of claims 1 to 3, wherein, in the azimuth angle dependence of the (110) plane of the polypropylene α-type crystal obtained by wide-angle X-ray diffraction measurement, the half width of the peak derived from the oriented crystal in the width direction is 21° or less. A biaxially oriented polypropylene film according to claim 1. The biaxially oriented polypropylene film according to any one of claims 1 to 4, wherein the biaxially oriented polypropylene film has a haze of 5.0% or less. The polypropylene resin constituting the biaxially oriented polypropylene film is a polypropylene homopolymer and/or a propylene copolymer containing 1 mol% or less of ethylene and/or an α-olefin component having 4 or more carbon atoms. 6. The biaxially oriented polypropylene film according to any one of 1 to 5. The biaxially oriented polypropylene film according to any one of claims 1 to 6, wherein the polypropylene resin constituting the biaxially oriented polypropylene film has a crystallization temperature of 105°C or higher and a melting point of 160°C or higher. The biaxially oriented polypropylene film according to any one of claims 1 to 7 , wherein the polypropylene resin constituting the biaxially oriented polypropylene film contains 35% by mass or more of components having a molecular weight of 100,000 or less.