JPH10264332A - Laminate film - Google Patents

Abstract

PROBLEM TO BE SOLVED: To form a film having a superior openability, heat-sealing property, transparency, not being likely to undergo surging during the film making period, and also having a high speed film making ability. SOLUTION: At least one surface of a base material film consisting of polyolefin or the like is laminated with a polyolefinic resin composition layer consisting of (a) a 100 pts.wt. ethylene-α-olefin random copolymer having a 70-90 mol.% content of a monomer unit based on ethylene, a 10-30 mol.% content of a monomer unit based on α-olefin except ethylene, and density of 0.85-0.90 g/cm<3> , (b) 10-100 pts.wt. propylene-α-olefin random copolymer having a 80-99 mol.% content of a monomer unit based on propylene, a 1-20 mol.% content of a monomer unit based on α-olefin except propylene, and (c) 10-50 pts.wt. polyethyene with a density of 0.91-0.04 g/cm<3> .

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a laminated film, and more particularly, to a laminated heat seal film having good openability.

[0002]

2. Description of the Related Art When packaging an article with a film, the film is heat-sealed. that time,
It is known to use a film in which a heat seal layer made of a polyolefin-based thermoplastic resin such as polypropylene or polyethylene is laminated on the surface of a base resin layer.

[0003] By the way, in such heat-sealing packaging, it is essential that the joints between the heat-sealed films are adhered to each other with such strength that they do not break during distribution. However, at the same time, it is also required that the bonding strength of the joint portion be such that the package can be easily opened by hand when the package is opened.

[0004] Furthermore, it is required that the joint can be opened cleanly at the time of opening. That is, in a laminated film having a heat seal layer made of the polyolefin-based thermoplastic resin, usually, when this bonding portion is to be peeled, smooth peeling does not occur at the welding interface between the films or inside the heat seal layer. In many cases, the base layer is torn during opening of the joint without separating the joint into the original films again. Such a phenomenon leads to poor appearance of the article at the time of opening,
Decrease the commercial value of the article. In addition, there is a danger that the torn portion becomes a starting point, the film is severely broken during opening, and the contents fall.

[0005]

Accordingly, it has been desired to solve the above-mentioned drawbacks and to develop a heat-sealing film having an excellent opening property and heat-sealing property. In view of the following, a) the content of monomer units based on ethylene is 70 to 90 mol%, and α other than ethylene is α.
-100 parts by weight of an ethylene-α-olefin random copolymer in which the content of monomer units based on olefin is 10 to 30 mol% b) The content of monomer units based on propylene is 80 to 99
Mol%, the content of monomer units based on α-olefins other than propylene is 1 to 20 mol%.
A laminated film in which a polyolefin resin composition layer composed of 10 to 100 parts by weight of an olefin random copolymer is laminated on at least one side of a base film has already been proposed (Japanese Patent Application No. 8-184328). This laminated film improves the above-mentioned problems and provides a film having good openability and heat sealability. However, at the time of film formation, the polyolefin resin composition is discharged from an extruder to take up a roll. In this case, there was a problem that surging easily occurred. Therefore, the laminated film cannot sufficiently cope with high-speed film formation and the like, and in this regard, the laminated film has room for improvement.

[0006]

Means for Solving the Problems The present inventors have intensively studied to solve the above problems. As a result, they have found that the above problems can be solved by blending a specific amount of low-density polyethylene with the polyolefin resin composition layer, and have completed the present invention.

That is, according to the present invention, a) the content of monomer units based on ethylene is 70 to 90 mol% and α other than ethylene is α.
-100 parts by weight of an ethylene-α-olefin random copolymer having a content of monomer units based on olefin of 10 to 30 mol% and a density of 0.85 to 0.90 g / cm ³ b) based on propylene The content of the monomer unit is 80 to 99.
Mol%, the content of monomer units based on α-olefins other than propylene is 1 to 20 mol%.
10 to 100 parts by weight of olefin random copolymer c) A polyolefin resin composition layer composed of 10 to 50 parts by weight of polyethylene having a density of 0.91 to 0.94 g / cm ³ is laminated on at least one surface of the base film. It is a laminated film comprising:

Hereinafter, the present invention will be described in more detail.

[0009] In the laminated film of the present invention, a specific ethylene-α-olefin random copolymer and a propylene-α-olefin random copolymer are contained in the components of the polyolefin resin composition layer. As a result, the laminated film of the present invention has excellent heat sealability, and also has extremely excellent openability when used as a heat seal film. It will peel off smoothly inside the polyolefin resin composition layer.

The ethylene-α-olefin random copolymer used in the present invention contains 70 to 90 mol%, preferably 73 to 87 mol% of monomer units based on ethylene, and a monomer unit based on another α-olefin. It contains 10 to 30 mol%, preferably 13 to 27 mol% of a body unit. The ethylene-α-olefin random copolymer having such a copolymerization ratio usually has a density of 0.85 to 0.90 g / c.
m is ^3. 70 mol% of monomer units based on ethylene
If the amount is less than that, it is not preferable because the slip property of the obtained laminated film is reduced. If the ethylene content is more than 90 mol%, the low-temperature heat sealability and openability of the obtained laminated film are undesirably reduced.

As other α-olefins, those having 3 to 12, preferably 3 to 8 carbon atoms, such as propylene, butene, pentene, methylbutene, hexene, methylpentene and octene are preferred. Melt flow rate (hereinafter abbreviated as MFR) is 0.1 to 50 in consideration of film forming property.
g / 10 minutes, preferably 0.5 to 30 g / 10 minutes. Regarding the crystallinity, considering the opening property, the 90% by weight elution temperature by a temperature-rise elution fractionation method using ortho-dichlorobenzene as a solvent is 60 ° C. or less, preferably 5 ° C. or less.
The temperature is preferably 5 ° C. or less, more preferably 50 ° C. or less. The weight-average molecular weight is preferably in the range of 250,000 to 350,000, and more preferably 30,000 to 300,000 in consideration of the opening property, heat seal strength, and extrusion processability.

The propylene-α-olefin random copolymer used in the present invention contains 80 to 99 mol%, preferably 85 to 98 mol% of monomer units based on propylene,
It contains 1 to 20 mol%, preferably 2 to 15 mol% of a monomer unit based on another α-olefin. If the monomer unit based on propylene is less than 80 mol%, the resulting laminated film is not preferable because the opening property of the laminated film is reduced. If it is more than 99 mol%, the transparency is undesirably reduced.

Other α-olefins include ethylene,
Those having 2 and 4 to 12, preferably 2 and 4 to 8 carbon atoms, such as butene, pentene, methylbutene, hexene, methylpentene and octene are good. Melt flow rate (hereinafter abbreviated as MFR) is determined in consideration of film forming property.
0.1 to 50 g / 10 min, preferably 0.5 to 30 g /
10 minutes is preferred. Also, differential scanning calorimetry (DSC)
The main peak in the range of 120 to 150 ° C., preferably 125 to 14
It is good to be in the range of 5 ° C. The weight-average molecular weight is 50,000 to 500,000, preferably 10
It is good that it is 10,000 to 350,000.

Further, according to the present invention, the density is 0.91 to 0.91.
0.94 g / cm ³ of polyethylene is used. Thereby, in the laminated film of the present invention, surging of the molten resin discharged from the extruder during film formation is reduced, and high-speed film forming property is improved. Further, the transparency of the polyolefin resin composition layer is also improved. On the other hand, if polyethylene having such a density is blended, the ethylene-α-
The effects of heat sealability and openability exhibited by the olefin random copolymer and the propylene-α-olefin random copolymer are favorably maintained. The density of the polyethylene is preferably 0.915 to 0.94 g / cm ³ . Here, when the density of polyethylene is smaller than 0.91, the effect of preventing surging is reduced, while
When it is larger than 0.94, the heat sealing property and the transparency are reduced in addition to the effect of preventing the surging. In addition, the polypropylene preferably has a melt flow rate (MFR) at 190 ° C. of 0.1 to 20 g / 10 minutes in consideration of film forming properties, and more preferably 0.5 to 15 g / 10 minutes.
More preferably, it is minutes. In addition, such a polyethylene generally has a main peak in a differential scanning calorimetry (DSC) of 115 to 130 ° C.

Specific examples of such polyethylene include ethylene homopolymers, ethylene-α-olefin copolymers, and mixtures thereof. In particular, high-pressure low-density polyethylene is preferable from the viewpoint of film forming workability.

In the laminated film of the present invention, the mixing ratio of the ethylene-α-olefin random copolymer, the propylene-α-olefin random copolymer and the polyethylene constituting the polyolefin resin composition layer is as follows: First, the propylene-α-olefin random copolymer is 10 to 100 parts by weight, preferably 15 to 80 parts by weight, based on 100 parts by weight of the olefin random copolymer.
Parts by weight, more preferably 15 to 65 parts by weight, and polyethylene is 10 to 50 parts by weight, preferably 20 to 50 parts by weight.
Parts by weight. When the blending amount of the propylene-α-olefin random copolymer is less than 10 parts by weight, the opening property of the obtained heat seal film decreases, and
If the amount is more than 0 parts by weight, the resulting heat-sealing film is not preferable because the opening property and transparency, particularly the opening property when the polyolefin resin composition layer is stretched, decrease. If the amount of the polyethylene is less than 10 parts by weight, the transparency of the obtained heat seal film decreases,
Further, the take-up surging becomes large, the high-speed film-forming property is lowered, and if it is more than 50 parts by weight, the resulting heat-sealing film is unpreferably open.

In the present invention, the above-mentioned components may be mixed by any method, but usually, the pellets of each copolymer are mixed with a mixer or the powder and / or pellets of each copolymer are heated. After mixing in a molten state, it is preferable to carry out the mixing with an extrusion kneader.

On the other hand, in the laminated film of the present invention, the substrate film on which the above-mentioned polyolefin resin composition layer is laminated on at least one side may be any type, but it is preferable to consider formability. Then, the main peak in DSC is 120 to 250 ° C., more preferably 13 to 250 ° C.
It is preferable that it is made of 0 to 170 ° C. Specific examples include polyolefin films such as homopolymers or copolymers of olefins such as ethylene, propylene, butene, and methylpentene, and among them, polypropylene is particularly preferable. These resins that can be used as the base material layer may be used alone or in combination of two or more.

As the polypropylene used for the base film, a homopolymer of propylene, 90 mol% or more of propylene and another α-olefin, for example, ethylene, 1-
Butene, 1-pentene, 1-hexene, 1-heptene,
A random copolymer or block copolymer with one or more of 10 mol% or less such as 4-methyl-1-pentene can be generally used. Melt flow rate (MF
R) is preferably in the range of 0.5 to 20 g / 10 minutes in consideration of film forming properties.

In the present invention, the base film may be a multilayer film of the above polyolefin film and another film. As such a multilayer film,
Resin recycling layer, polyvinyl alcohol, ethylene
Examples thereof include those in which a layer having a gas barrier property such as a saponified vinyl acetate copolymer or a silica vapor-deposited layer is provided as an intermediate layer.

Next, in the laminated film of the present invention, a polyethylene and / or propylene-based monomer having a density of 0.91 to 0.95 g / cm ³ is further provided on the surface of the polyolefin resin composition layer. Unit: 85 to 9
An outer surface layer made of a propylene-based random copolymer containing 9 mol% may be laminated and used. When the laminated film of the present invention is used as a heat seal film, the outer surface layer acts alone or melts together with the polyolefin resin composition layer to act as a heat seal layer. In addition, when this layer is located on the outer surface, the laminated film has further improved slipperiness. Furthermore, when the propylene-based random copolymer is used as the resin of the outer surface layer, the laminated film has excellent scratch resistance.

Here, the polyethylene needs to have a density of 0.91 to 0.95 g / cm ³ in consideration of the slipperiness, transparency, heat sealability and the like of the film. More preferably, it is 915 to 0.94 g / cm ³ . Also, considering film forming properties, etc.,
The melt flow rate (MFR) at 90 ° C. is 0.
It is preferably 1 to 20 g / 10 min, and more preferably 0.5 to 15 g / 10 min. In addition, such polyethylene is generally used for differential scanning calorimetry (D
Generally, the main peak in SC) is 115 to 130 ° C.

Specific examples of such polyethylene include ethylene homopolymers, ethylene-α-olefin copolymers, and mixtures thereof. Particularly, from the viewpoint of stretchability, a linear low-density polyethylene which is an ethylene-α-olefin copolymer is preferable.

Here, if the density of polyethylene is less than 0.91, the slipperiness of the film becomes insufficient. on the other hand,
When this density exceeds 0.95, the heat sealability and transparency of the film are reduced.

On the other hand, when the monomer unit based on propylene is 8
As the monomer other than the propylene-based monomer unit in the propylene-based random copolymer containing 8 to 99 mol%, a unit based on another known monomer copolymerizable with propylene can be employed without limitation. . Preferably, ethylene,
Α having 2 and 4 to 12 carbon atoms, such as butene, pentene, methylbutene, hexene, methylpentene, octene, etc.
-Monomer units based on olefins, and these may be used alone or in combination of two or more. As such a propylene-based random copolymer, specifically, a propylene-ethylene copolymer, a propylene-ethylene-butene terpolymer, a propylene-butene copolymer, a propylene-hexene copolymer, or a mixture thereof A mixture or the like can be used.

Here, the content ratio of the monomer unit based on propylene in the propylene random copolymer is 88 to 88%.
It needs to be 99 mol%, preferably 90-98 mol%. When the content of the propylene-based monomer unit is less than 88 mol%, the film has insufficient lubricating properties. On the other hand, when the content ratio of the monomer unit based on propylene exceeds 99 mol%, the heat sealability of the film is undesirably reduced. In consideration of film forming properties, the propylene random copolymer has a melt flow rate (MFR) at 230 ° C. of 0.1 to 20.
g / 10 minutes, more preferably 0.5 to 1
More preferably, it is 5 g / 10 minutes. Further, this propylene-based random copolymer was subjected to differential scanning calorimetry (D
The main peak in SC) is preferably in the range of 125 to 155 ° C, preferably 130 to 150 ° C.

The layer made of the polyethylene and / or the propylene random copolymer may be provided as two or more layers.

In the present invention, the outer surface layer, the polyolefin resin composition layer and the base film constituting the laminated film may contain, if necessary, an antistatic agent, an antifogging agent, an antiblocking agent, an antioxidant, Known additives such as a stabilizer, a crystal nucleating agent, a lubricant, a surfactant for the purpose of imparting lubricity and imparting an anti-blocking property may be blended and used. Further, to the extent that the physical properties of the present invention are not impaired,
Other resins can be mixed. The resin to be mixed is not particularly limited, but, for example, propylene, ethylene,
Homopolymers or copolymers of olefins such as butene, or mixtures of two or more of these are preferred. The addition amount is preferably 20% by weight or less, more preferably 15% by weight or less. In particular, in the outer surface layer, as another resin, a propylene-butene random copolymer having a butene content of 10 to 30 mol%, a butene-propylene random copolymer having a propylene content of 10 to 30 mol%, and a density of 0 .85 or more and 0.9
Less than one ethylene-α-olefin random copolymer is preferred.

In the present invention, the thickness of the laminated film is not particularly limited.
m and preferably 15 to 120 μm. The thickness of the polyolefin resin composition layer is generally appropriately selected from the range of 0.1 to 15 μm.
It is preferably from 5 to 10 μm. When the outer surface layer is provided, the thickness of the layer is preferably 0.1 to 10 μm in consideration of slipperiness, film forming property, and the like,
More preferably, it is 0.5 to 5 μm.

Next, the method of forming the laminated film of the present invention is not particularly limited, and it may be manufactured by any method. In general, the polyolefin resin powder or pellets constituting the polyolefin resin composition layer, alone or in some cases after sufficient mixing with other resin powder or pellets, and co-extruded with the resin component of the base film Quenching on a temperature-controlled chill roll to form a film without stretching, and then stretching uniaxially or biaxially, or melt-extruding one layer of resin to stretch uniaxially, and then layer another layer of resin onto it. A method of melt extrusion and stretching in a direction substantially perpendicular to the direction of the uniaxial stretching is employed. As an example of longitudinal uniaxial stretching, generally, a film is passed between a roll rotating at a low speed at the frontmost portion and a roll rotating at a high speed at the rearmost portion, and is stretched by the rotation speed ratio of both rolls. One side
As an example of the axial stretching, it is preferable to perform the stretching by a tenter method. Further, longitudinal and horizontal sequential biaxial stretching, simultaneous biaxial stretching, and the like can be performed by the methods described above. The stretching magnification is 5 in area magnification.
６０60 times, and more preferably 30 to 50 times.

Although the above is the case of the flat shape, it is also possible to stretch the tubular material uniaxially, biaxially and simultaneously biaxially by an inflation method. In this case, the raw material is heated to, for example, 80 to 150 ° C., and pressurized air is sent into the tubular film to form a film without stretching, or stretch uniaxially in the longitudinal or transverse direction, or simultaneously stretch in the longitudinal or transverse direction. What is necessary is just to carry out axial stretching.

In these molding methods, considering the transparency and elastic modulus (rigidity of the film) of the laminated film, etc.
Axial stretching is preferred.

When obtaining a laminated film in which an outer surface layer made of polyethylene and / or a propylene-based random copolymer is laminated on the surface of the polyolefin resin composition layer, co-extrusion of the film is performed in the above-described layer configuration. In this case, the molding may be performed in the same manner as described above.

[0034]

The laminated film of the present invention is particularly suitable for a heat seal film, and provides a heat seal film which not only forms a structure having excellent sealing reliability by heat sealing but also has an excellent opening property. I do. In particular, when the fused joint is peeled off, the base layer is not torn and the films are favorably peeled off at the interface and the polyolefin resin composition layer. In addition, during film formation, when the polyolefin resin composition is discharged from an extruder and taken up by a roll, surging does not easily occur, and high-speed film forming properties are excellent. Further, the polyolefin resin composition layer has good transparency, and when a material having good transparency such as polypropylene is used as the base film, the film becomes excellent in transparency. Then, by laminating a layer made of polyethylene and / or a propylene-based random copolymer as the outer surface layer, the sliding property and the scratch resistance are further improved.

[0035]

EXAMPLES The present invention will be described below with reference to examples and comparative examples, but the present invention is not limited to these examples.

The polyolefin resins used as the base film and laminated film raw materials in the examples and comparative examples are those shown in Table 1.

[0037]

[Table 1]

The measuring methods used in the following Examples and Comparative Examples were implemented by the following methods.

(1) Weight average molecular weight (Mw) Measured by GPC (gel permeation chromatography). SSC-7100 manufactured by Senshu Science Co., Ltd.
GPC apparatus uses O-dichlorobenzene as a solvent and
Performed at 45 ° C. The column is Showa Denko UT-807,
Two UT-806M and four UT-802.5 were connected in series and used. A calibration curve was prepared using standard polystyrene, and the weight average molecular weight was measured.

(2) Copolymer Composition Using a JNM-GSX-270 apparatus manufactured by JEOL Ltd.,
Ortho-dichlorobenzene / heavy benzene (volume ratio 90/1
Calculated from ¹³ C-NMR spectrum measured at 120 ° C. using 0) as a solvent.

(3) Melt flow rate (MFR) Measured according to JIS K7210.

(4) Measurement of elution temperature by temperature rise elution fractionation (TREF) Automatic TREF device SSC-730 manufactured by Senshu-Kagaku Co., Ltd.
The measurement was performed under the following conditions using 0ATREF.

Solvent: ortho-dichlorobenzene Flow rate: 150 ml / hour Heating rate: 4 ° C./hour Detector: Infrared detector Measurement wave number: 3.41 μm Column: “Packed column 30φ” manufactured by Senshu-Chemical Co., Ltd. 30 mmφ × 300 mm Concentration: 1 g / 120 ml Injection amount: 100 ml In this case, the sample solution in the column was introduced at 145 ° C., and then cooled to 10 ° C. at a rate of 2 ° C./hour to adsorb the sample polymer on the surface of the filler. Thereafter, by raising the column temperature under the above conditions, the polymer eluted at each temperature was obtained.
The concentration was measured with an infrared detector.

(5) Measurement of main peak by DSC After weighing about 5 to 6 mg of a sample, the sample was sealed in an aluminum pan, and the temperature was changed from room temperature to 235 ° C. or 270 ° C. in a nitrogen flow of 20 ml / min by a differential calorimeter. Raise the temperature and at these temperatures
Hold for 0 minutes, then cool to room temperature at 10 ° C / min. Thereafter, the temperature of the main peak was measured by a melting curve obtained at a heating rate of 10 ° C./min.

(6) Transparency The haze value of the film was measured according to JIS-K6714.

(7) Low-temperature heat-sealing property (heat-sealing starting temperature)
Using a heat seal bar, set each temperature (from 80 ° C to 1
(Measured every 5 ° C up to 55 ° C)
A sample having a width of 15 mm was cut out from a sample sealed under the conditions of kg / cm 2 and a heat sealing time of 1.0 second, and measured at a tensile speed of 500 mm / min using a tensile tester.
The results were average values of five samples. From the heat seal curve obtained by the above method, the heat seal strength was 300 g /
The temperature of 15 mm was set as the heat sealing start temperature.

(8) Slipperiness After film formation, ASTM-D after curing at 40 ° C. for 2 days
It measured according to the dynamic friction coefficient measuring method of -1894.

(9) Opening property Heat seal starting temperature and further 5 ° C. and 10 ° C.
For samples heat-sealed at high temperatures, 10
Using a tensile tester for each sample, a tensile speed of 500 mm /
In a total of 30 samples measured in minutes, the bonding portion was not peeled off at the interface or the surface layer portion of both films, and the number was determined by the number of base films of one of the films being torn and separated. The criteria are as follows.

[0049]

[Table 2]

(10) Scratch Resistance (Scratch Haze) In order to evaluate the easiness of scratching when rubbing the films, two films were prepared and one of the films (20 ×
30 cm) was fixed as the lower film. The other film is used as the upper film, and the diameter of the upper film is 10 cm.
The lower film was brought into contact with a load of 4.6 kg on the area of the circle of, and the upper film was horizontally rubbed five times back and forth for 20 cm. The haze value before and after performing the above operation was measured, and it was evaluated that the smaller the haze value, the less likely it was to be damaged. The criteria are as follows.

[0051]

[Table 3]

(11) High-speed film-forming property The raw material resin to be laminated was extruded into a sheet while being heated and melted using a T-die extruder, bonded to a base film on a chill roll, and solidified by cooling. The chill roll take-up speed was 20, 30, 50, 70, and 90 m / min, and the thickness variation (surging) of the cooling sheet was measured. As the take-up speed of the resin with poor spreadability increased, a large thickness variation periodically occurred with respect to the sheet thickness.

[0053]

[Table 4]

Examples 1 to 6 Using a resin shown in A in Table 1 as a base film and extruding it into a sheet under heating and melting at 280 ° C. using a T-die extruder,
After cooling and solidifying on a chill roll, it was stretched 4.5 times with a heated roll stretching machine to obtain a uniaxially stretched sheet. Then
The resins shown in Tables 1 and 5 were heated at 260 ° C. using a T-die extruder.
Extruded into a sheet while heating and melting at a chill roll (chill roll take-off speed 20 m / mi)
The two-layer sheet was obtained by laminating in n), and subsequently stretched 9 times by a horizontal stretching machine. Separately, the high-speed film forming property in the above-mentioned lamination was measured.

The thickness, haze, heat sealability, openability and slipperiness of the obtained film were measured, and the results are shown in Table 6. The raw resin constituting the polyolefin resin composition layer had an average particle size of 4 parts by weight based on 100 parts by weight of the raw resin.
0.5 parts by weight of micron spherical polymethyl methacrylate particles and 0.5 parts by weight of erucamide were added.

Example 7 Except that the resin shown in B in Table 1 was used as the base film,
A laminated film was obtained in exactly the same manner as in Example 1. The thickness of the obtained film, haze, heat sealability, openability,
The slip property and the high-speed film-forming property of the polyolefin resin composition were measured, and the results are shown in Table 6.

Example 8 The resin shown in A in Table 1 was used for a base film, and the resin and the resin for lamination shown in Tables 1 and 5 were heated and melted at 260 ° C. using a two-layer T-die extruder. Lower co-extrusion, tenter method 2
The film was stretched 4 times vertically and 8 times horizontally by an axial stretching machine to obtain a laminated film. The thickness, haze, heat sealability, openability, slipperiness, and high-speed film forming property of the laminated resin of the obtained film were measured. The results are shown in Table 6. The raw resin constituting the polyolefin resin composition layer contains 100 raw resin.
0.5 part by weight of spherical polymethyl methacrylate particles having an average particle size of 4 μm and 0.5 part by weight of erucamide
Parts by weight were added.

Example 9 The resin shown in A in Table 1 was used for a base film, and the resin and the resin for lamination shown in Table 1 were heated and melted at 260 ° C. using a two-layer T-die extruder. It was extruded and cooled and solidified on a chill roll to obtain a non-stretched two-layer film. The thickness, haze, heat sealability, openability, slipperiness, and high-speed film forming property of the laminated resin of the obtained film were measured. The results are shown in Table 6. In the raw resin constituting the polyolefin resin composition layer, spherical polymethyl methacrylate particles having an average particle diameter of 4 μm were contained in 0.7 parts by weight per 100 parts by weight of the raw resin.
Parts by weight, and 0.5 parts by weight of erucamide.

Comparative Examples 1 to 7 In Example 1, a film was obtained in the same manner as in Example 1, except that the resins shown in Tables 1 and 5 were used as the base film and the resin for the polyolefin resin composition layer. Was.
Measure the thickness of the obtained film, haze, heat sealability, openability, slipperiness and high-speed film-forming properties of the laminated resin,
The results are shown in Table 6. In the raw resin constituting the polyolefin resin composition layer, 0.5 parts by weight of spherical polymethyl methacrylate particles having an average particle diameter of 4 μm and 0.5 parts by weight of erucamide were added to 100 parts by weight of the raw resin. Was added.

[0060]

[Table 5]

[0061]

[Table 6]

Examples 10 to 14 Using a resin shown in A in Table 1 as a base film, a T-die extruder was used to extrude a sheet at 280 ° C. while heating and melting.
After cooling and solidifying on a chill roll, it was stretched 4.5 times with a heated roll stretching machine to obtain a uniaxially stretched sheet. Then
The resins shown in Tables 1 and 7 were converted to 26 using a two-layer T-die extruder.
Under heat melting at 0 ° C., co-extruded into a sheet form, and rolled on the uniaxially stretched sheet and roll (chill roll take-off speed 20 m / m
in) to obtain a three-layer sheet, which was subsequently stretched 9 times with a horizontal stretching machine. Separately, the high-speed film forming property in the above-mentioned lamination was measured.

The thickness, haze, heat sealability, openability, slipperiness and scratch resistance of the obtained film were measured. The results are shown in Table 8. The raw material resin constituting the outer surface layer contained an average particle size of 4 with respect to 100 parts by weight of the raw material resin.
0.5 parts by weight of micron spherical polymethyl methacrylate particles and 0.5 parts by weight of erucamide were added.

Comparative Examples 8 to 11 The same procedures as in Example 1 were carried out except that the resins shown in Tables 1 and 7 were used as the base film and the resin for lamination.
A film was obtained in the same manner as described above. The thickness, haze, heat sealability, opening property, slipping property, scratch resistance and high-speed film forming property of the laminated resin of the obtained film were measured. The results are shown in Table 8. In the raw material resin constituting the outer surface layer, 0.5 parts by weight of spherical polymethyl methacrylate particles having an average particle diameter of 4 μm and 0.5 parts by weight of erucamide were added to 100 parts by weight of the raw material resin. .

[0065]

[Table 7]

[0066]

[Table 8]

Continued on the front page (51) Int.Cl. ⁶ Identification code FI // (C08L 23/08 23:14 23:06)

Claims (2)

[Claims] 1. A) The content of monomer units based on ethylene is 70 to 90 mol%, the content of monomer units based on α-olefins other than ethylene is 10 to 30 mol%, and the density is 0. Ethylene-α- is 85 to 0.90 g / cm ³
100 parts by weight of olefin random copolymer b) The content of monomer units based on propylene is 80 to 99.
Mol%, the content of monomer units based on α-olefins other than propylene is 1 to 20 mol%.
10 to 100 parts by weight of olefin random copolymer c) A polyolefin resin composition layer composed of 10 to 50 parts by weight of polyethylene having a density of 0.91 to 0.94 g / cm ³ is laminated on at least one surface of the base film. Laminated film. 2. Polyethylene having a density of 0.91 to 0.95 g / cm ³ and / or propylene containing 85 to 99 mol% of a monomer unit based on propylene, on the surface of the polyolefin resin composition layer. The laminated film according to claim 1, wherein an outer surface layer made of a system random copolymer is laminated.