JP3330863B2 - Polyester film for metal plate lamination processing - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyester film for laminating and forming a metal plate, and more particularly, it shows excellent formability when laminating to a metal plate and performing can forming such as drawing. The present invention relates to a polyester for metal plate lamination molding capable of producing metal cans, such as beverage cans, food cans, and the like, having excellent properties, retort resistance, flavor preserving properties, impact resistance, and the like.

[0002]

2. Description of the Related Art Metal cans are generally coated to prevent corrosion on the inner and outer surfaces, but recently, for the purpose of simplifying the process, improving hygiene, and preventing pollution, rust prevention is performed without using an organic solvent. Development of a method for obtaining the property has been advanced, and as one of the methods, coating with a thermoplastic resin film has been attempted.

[0003] That is, a method of laminating a thermoplastic resin film on a metal plate of tin, tin-free steel, aluminum or the like, followed by drawing or the like is being studied.

As the thermoplastic resin film, it is gradually becoming clear that a copolymerized polyester film is suitable in terms of moldability, heat resistance, impact resistance, and taste and fragrance retention. However, this polyester film does not necessarily show sufficient flavor retention and aroma when the beverage contains extremely important tastes such as green tea and mineral water which is required to be tasteless and odorless. Is sensed.

On the other hand, Japanese Patent Application Laid-Open No. Hei 6-116376 proposes a polyester film for forming a metal plate having an improved flavor, comprising a copolymerized polyester containing a specific amount of an alkali metal element and a germanium element. ing. However, when this film is used, it shows excellent flavor and fragrance retention in the process where heat is not applied at the stage of filling the contents such as a cold back system, but at the stage of filling the contents such as retort treatment. In the step in which the heat treatment is performed, sufficient flavor and fragrance retention cannot always be obtained.

[0006]

SUMMARY OF THE INVENTION Accordingly, the present invention solves the above-mentioned problems of the prior art, and provides the excellent moldability, heat resistance, impact resistance and retort resistance of the copolymerized polyester film. It is an object of the present invention to provide a polyester film for metal plate laminating processing, which has an improved flavor preserving property, particularly, a preserving property after retort treatment.

[0007]

Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, among copolymerized polyesters, ethylene terephthalate is a main repeating unit and has a specific melting point. By using a polymerized polyester and having a specific glass transition temperature, dynamic viscoelasticity, and a film containing a specific porous silica, the flavor and flavor retention, particularly after retort treatment, is remarkable. It has been found that the present invention has been improved, and the present invention has been completed.

That is, the present invention has a melting point of 210 to 24.
Naphthalene dicarboxylic acid having 5 ° C and Tg of 78 ° C to 83 ° C
6-18% by mole of acid based on all dicarboxylic acid components
A biaxially stretched film made of the copolymerized polyethylene terephthalate, wherein the maximum temperature peak temperature (Te) of the loss modulus of the film and the glass transition temperature (Tg) in DSC measurement are represented by the following formulas (1) and (2). Satisfied
And a metal plate containing an aggregate of primary particles having an average particle diameter of 0.001 to 0.1 μm and containing porous silica particles having a pore volume of 0.5 to 2.0 ml / g. It is a polyester film for lamination molding.

[0009]

## EQU2 ## 83 ≧ Tg ≧ 78 (1) Te−Tg ≦ 30 (2) (where Tg is DS after heating and melting at 290 ° C. and quenching)
The glass transition temperature (° C.) and Te in the C measurement are the highest peak temperature (° C.) of the loss modulus of the film. )

When the copolymerized polyethylene terephthalate film is extracted with ion-exchanged water at 121 ° C. for 2 hours, the amount of extraction is preferably 0.5 mg or less per square inch.

[0011]

BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, among various copolyesters, while retaining excellent heat resistance, impact resistance and retort resistance, the flavor and fragrance preservation property, particularly the preservation after retort treatment, is maintained. The melting point is 21 because the flavor retention can be improved.
Naphthalene range of 0 to 245 ° C and Tg of 78 ° C to 83 ° C
Carboxylic acid is 6 to 18 mol based on all dicarboxylic acid components
% Copolymerized polyethylene terephthalate.
A biaxially stretched film is used.

The copolymerized polyethylene tereph according to the present invention
Talate is a copolymer component other than naphthalenedicarboxylic acid
May be copolymerized, and the copolymerization component may be a dicarboxylic acid component or a diol component. Hereinafter, copolymerized polyethylene
Renterephthalate is simply called copolymerized polyester.
There is.

The dicarboxylic acid component includes aromatic dicarboxylic acids such as isophthalic acid, phthalic acid, and 2,6-naphthalenedicarboxylic acid; aliphatic dicarboxylic acids such as adipic acid, azelaic acid, sebacic acid and decane dicarboxylic acid; Alicyclic dicarboxylic acids such as cyclohexanedicarboxylic acid can be exemplified.
Examples thereof include aliphatic diols such as -butanediol, 1,6-hexanediol, and diethylene glycol; alicyclic diols such as 1,4-cyclohexanedimethanol; and aromatic diols such as bisphenol A. These can be used alone or in combination of two or more.

The proportion of the copolymer component depends on the kind thereof, and as a result, the melting point of the polymer is in the range of 210 to 245 ° C., preferably 215 to 240 ° C. If the melting point is lower than 210 ° C., the heat resistance will be poor. On the other hand, when the melting point exceeds 245 ° C., the crystallinity of the polymer is too large and the moldability is impaired.

Here, the melting point of the copolyester was measured by Du Pont Instruments 910.
A method in which a melting peak is determined at a heating rate of 20 ° C./min using DSC. The sample amount is about 20 mg.

Further, the intrinsic viscosity (orthochlorophenol, 35 ° C.) of the copolymerized polyester used in the present invention is preferably 0.52 to 1.50, more preferably 0.57 to 1.00, and particularly preferably. Is 0.60
0.80. If the intrinsic viscosity is less than 0.52, the impact resistance may be insufficient, which is not preferable. On the other hand,
If the intrinsic viscosity exceeds 1.50, the moldability may be impaired.

The copolymerized polyester in the present invention is not limited by its production method, but includes terephthalic acid,
A method of subjecting ethylene glycol and a copolymer component to an esterification reaction, and then subjecting the obtained reaction product to a polycondensation reaction to a desired degree of polymerization to give a copolymerized polyethylene terephthalate, or dimethyl terephthalate, ethylene glycol and Preferable examples include a method of subjecting a copolymer component to a transesterification reaction and then subjecting the obtained reaction product to a polycondensation reaction until a desired degree of polymerization is obtained to obtain a copolymerized polyethylene terephthalate. Further, the copolymerized polyethylene terephthalate obtained by the above method (melt polymerization) can be converted into a polymer having a higher degree of polymerization by a polymerization method in a solid state (solid state polymerization) if necessary.

If necessary, additives such as an antioxidant, a heat stabilizer, a viscosity modifier, a plasticizer, a hue improver, a lubricant, a nucleating agent, and an ultraviolet absorber may be added to the copolymerized polyester. it can.

The catalyst used in the polycondensation reaction includes:
Antimony compounds (Sb compounds), titanium compounds (Ti
Compounds), germanium compounds (Ge compounds), etc., among which titanium compounds and germanium compounds are preferred in view of the taste and fragrance retention of the film. As the titanium compound, for example, titanium tetrabutoxide,
Preference is given to titanium acetate. As the germanium compound, (a) amorphous germanium oxide,
(B) fine crystalline germanium oxide, (iii) a solution of germanium oxide dissolved in glycol in the presence of an alkali metal or an alkaline earth metal or a compound thereof,
(D) A solution obtained by dissolving germanium oxide in water is preferred. Furthermore, when an antimony compound and a titanium compound are used in combination, along with the improvement of the taste and fragrance retention,
This is preferable because the cost can be reduced.

The polyester film of the present invention is used in a state of being biaxially stretched and heat set. At this time, the highest temperature peak temperature (Te) of the loss modulus of the polyester film
And the glass transition temperature (Tg) in the DSC measurement must satisfy the following expressions (1) and (2).

[0021]

(3) 83 ≧ Tg ≧ 78 (1) Te−Tg ≦ 30 (2) (where Tg is DS after heating and melting at 290 ° C.-quenching)
The glass transition temperature (° C.) and Te in the C measurement are the highest peak temperature (° C.) of the loss modulus of the film. )

When the Tg of the film is less than 78 ° C., the heat resistance becomes poor, and the flavor and aroma retention after retorting deteriorates. For this reason, it is preferable to use, as the copolymerization component of the copolymerized polyester, at least one component that does not change or increases the glass transition temperature when the proportion of the copolymerization component is increased. As a component that increases the glass transition temperature when the proportion of the copolymer component is increased, 2,6-dicarboxylic acid component is used.
Naphthalenedicarboxylic acid has a diol component of 1,
Preferred is 4-cyclohexanedimethanol.

Here, the Tg of the polyester was measured by placing a 20 mg film sample in a pan for DSC measurement,
After heating and melting for 5 minutes on a heating stage, the sample pan was quickly cooled and solidified on an aluminum foil spread on ice,
A method of determining a glass transition point at a heating rate of 20 ° C./min using on Instruments 910 DSC.

Further, when the value of Te-Tg exceeds 30, the molecular orientation and the crystallinity of the film become too high, so that the formability is remarkably reduced. Although the value of Te depends on the copolymerization component and the copolymerization amount, a method of adjusting the film forming conditions, particularly the biaxial stretching ratio, the stretching temperature, and the heat setting temperature, is preferably mentioned.

Here, Te is determined at a measurement frequency of 10 Hz and a dynamic displacement of ± 25 × 10 ⁻⁴ cm using a dynamic viscoelasticity measuring device.

Further, the polyester film of the present invention comprises:
It is necessary to contain porous silica particles which are aggregated particles. When spherical or amorphous silica particles are contained as in the prior art, a remarkable effect of improving the flavor and fragrance retention cannot be obtained.

The average particle size of the primary particles constituting the porous silica particles needs to be in the range of 0.001 to 0.1 μm. If the average particle size of the primary particles is less than 0.001 μm, ultrafine particles are generated by crushing at the slurry stage, which forms aggregates, causes pinholes, and deteriorates moldability, so that it is inappropriate. is there. On the other hand, if the average particle size of the primary particles exceeds 0.1 μm, the porosity of the particles will be lost, and as a result, the flavor and fragrance retention will not be improved.

Further, the porous silica particles have a pore volume of 0.5 to 2.0 ml / g, preferably 0.6 to 1.
It needs to be in the range of 8 ml / g. If the pore volume is less than 0.5 ml / g, the porosity of the particles will be lost, and the effect of improving the taste and fragrance retention will be lost. On the other hand, if the pore volume is larger than 2.0 ml / g, agglomeration tends to occur due to crushing, which causes pinholes and deteriorates moldability.

The particle size and amount of the porous silica are as follows:
What is necessary is just to determine from the winding property of a film, pinhole resistance, and flavor retention. Usually, the average particle size of the porous silica particles is preferably in the range of 0.1 to 5 μm, preferably 0.3 to 3 μm, and the amount added is 0.01 to 1% by weight, preferably 0.02% by weight. Preferably, it is in the range of .about.0.5% by weight.

The porous silica particles used in the present invention form agglomerated particles. The polyester film of the present invention has a size of 50 μm or more in the number of coarse agglomerated particles.
Number / m ² or less, preferably 5 / m ² or less, more preferably 3 / m ² or less. If the number of coarse aggregated particles having a size of 50 μm or more is too large, pinholes are likely to be generated, and the moldability tends to be poor.

In order to reduce the number of coarse agglomerated particles, an average opening of 10 to 30 μm, preferably 15 μm, of a stainless steel fine wire having a diameter of 15 μm or less is used as a filter at the time of film formation.
It is preferable to filter the molten polymer using a nonwoven fabric type filter having a size of 25 μm.

The porous silica particles are generally used at the time of the reaction for producing the polyester, for example, at any time during the transesterification reaction or polycondensation reaction in the case of transesterification, or in the case of the direct polymerization method. At times, it is added to the reaction system (preferably as a slurry in glycol). In particular, it is preferable to add porous silica particles to the reaction system at the beginning of the polycondensation reaction, for example, until the intrinsic viscosity reaches about 0.3.

The surface roughness (Ra) of the polyester film of the present invention is 15 in terms of the winding property of the film and the flavor and fragrance retention.
nm or less, particularly preferably 4 to 15 nm.

The surface roughness (Ra) of the film is J
This is the center line average roughness determined according to IS-B0601, and a portion of the measured length L is extracted from the film surface roughness curve in the direction of the center line, the center line of the extracted portion is defined as the X axis, and the longitudinal magnification Is the Y axis, the roughness curve Y = f
When represented by (x), a value (Ra:
nm) is defined as the film surface roughness.

[0035]

(Equation 4)

In the present invention, when the reference length is 2.5 mm, 5
The number is measured, and Ra is represented as an average of four values excluding one from the larger value.

Since the polyester film of the present invention is used especially for food cans or beverage cans, it is better that the amount of substances eluted or scattered from the film is smaller, but it is substantially impossible to eliminate those substances at all. Impossible. Therefore, in order to use it for food cans or beverage cans, for example, the extraction amount per square inch of the film when extracted with ion-exchanged water at 121 ° C. for 2 hours is 0.5 m.
g or less, more preferably 0.1 mg or less.

In order to reduce the amount of extraction, the glass transition temperature of the polyester film may be increased.
The glass transition temperature of a polyester film is determined by the glass transition temperature and the degree of orientation of the polymer constituting the film, but if the degree of orientation is increased, the moldability deteriorates. Preferably, it is higher.

The refractive index of the polyester film in the thickness direction is preferably from 1.500 to 1.545, more preferably from 1.505 to 1.530. If the refractive index is too low, the moldability will be insufficient, while if it is too high, the structure will be close to amorphous, and the heat resistance may decrease.

Here, the refractive index in the thickness direction of the polyester film is measured with a monochromatic NaD line by attaching a polarizing plate analyzer to the eyepiece side of the Abbe refractometer. The mounting solution uses methylene iodide, and the measurement temperature is 25 ° C.

The polyester film of the present invention preferably has a thickness of 6 to 75 μm. Further, it is preferably from 8 to 75 μm, particularly preferably from 10 to 50 μm. 6 μm thick
If it is less than 75%, breakage or the like tends to occur during processing, while
Those exceeding μm are excessive quality and uneconomical.

As a metal plate to which the polyester film of the present invention is bonded, in particular, a metal plate for can making, a plate of tin, tin-free steel, aluminum or the like is suitable.
The bonding of the polyester film to the metal plate can be performed, for example, by the following method. The metal plate is heated to a temperature equal to or higher than the melting point of the film, the film is bonded, and then rapidly cooled, and the surface layer (thin layer) of the film in contact with the metal plate is made amorphous and adhered. An adhesive layer is primer-coated on the film in advance, and this surface is bonded to a metal plate. As the adhesive layer, a known resin adhesive, for example, an epoxy adhesive, an epoxy-ester adhesive, an alkyd adhesive, or the like can be used.

[0043]

The present invention will be further described with reference to the following examples.
The characteristics in the examples were measured by the following methods. (1) Intrinsic viscosity of polyester Measured in orthochlorophenol at 35 ° C.

(2) Melting point of polyester Du Pont Instruments 910 D
A method in which a melting peak is determined at a heating rate of 20 ° C./min using SC. The sample amount is 20 mg.

(3) Glass transition temperature of polyester (T
g) 20 mg of a film sample was placed in a pan for DSC measurement, heated and melted for 5 minutes on a 290 ° C. heating stage, and then rapidly cooled and solidified on an aluminum foil spread on ice, and then Du Pont Instruments 910 was prepared.
A method in which the glass transition point is determined at a heating rate of 20 ° C./min using DSC.

(4) Maximum peak temperature of loss elastic modulus of film (Te) The loss elastic modulus was determined at a measurement frequency of 10 Hz and a dynamic displacement of ± 25 × 10 ⁻⁴ cm using a dynamic viscoelasticity measuring apparatus. The peak temperature at this time is shown.

(5) Particle Size The average particle size of the primary particles is determined by dispersing silica powder so that the individual particles do not overlap as much as possible, and depositing a metal vapor-deposited film on the surface with a thickness of 20 to 30 nm using a gold sputtering apparatus. Formed, using a scanning electron microscope for 10,000-3000
Observation was performed at a magnification of 0, and image processing was performed using Luzex 500 manufactured by Nippon Regulator Co., Ltd., and the average particle diameter was determined from 100 particles. The average particle size of particles that are aggregates of primary particles is
The diameter of 50% of the integrated volume fraction in the equivalent spherical distribution measured by the centrifugal sedimentation type particle size distribution analyzer is defined as the average particle size.

(6) Pore Volume Using Autosorb-1 manufactured by Cantachrome Co., Ltd., the nitrogen pressure was measured by a constant volume method. Assuming that the pores of the powder were filled with nitrogen, the relative pressure = The pore volume of the powder is determined from the nitrogen adsorption at 0.998.

(7) Deep drawing workability The film was heated to a temperature equal to or higher than the melting point of polyester.
Affixed to both sides of 25mm tin-free steel, water-cooled, cut into a circular shape of 150mm diameter, deep-drawn in four stages using a drawing die and a punch, and a 55mm diameter sideless seamless container (hereinafter abbreviated as can) )created. The following observations and tests were performed on the cans, and the cans were evaluated according to the following criteria.

Deep drawing workability -1 ：: No whitening or breakage is observed in the film processed without any abnormality. Δ: Whitening is observed at the top of the film can. X: Film breakage is observed in a part of the film. Deep drawing workability-2 ○: Processed without any abnormality, rust prevention test of film surface in can (1% NaCl aqueous solution was put in the can, electrodes were inserted, and a voltage of 6 V was applied with the can body as an anode. The current value at the time is measured, and is 0.2 mA or less in the ERV test. ×: No abnormality was found in the film, but the current value was 0.2 mA or more in the ERV test. When the energized portion was observed under magnification, pinhole-shaped cracks starting from the coarse lubricant were observed in the film.

(8) Impact Resistance For cans with good deep drawing, pour water completely, cool to 0 ° C., drop 10 pieces for each test from a height of 30 cm onto a PVC tile floor. As a result of the ERV test in the can, the results were as follows: ○: 0.2 mA or less for all 10 samples. C: 0.2 mA or more for 1 to 5 pieces. ×: 0.2 mA or more for 6 or more pieces, or cracks of the film were already observed after dropping.

(9) Heat Embrittlement Resistance The can which had been successfully deep drawn was heated and maintained at 200 ° C. for 5 minutes, and then subjected to the impact resistance evaluation described in (8). It was 0.2 mA or less. C: 0.2 mA or more for 1 to 5 pieces. X: The film was 0.2 mA or more for 6 or more pieces, or cracking of the film was already observed after heating at 200 ° C. for 5 minutes.

(10) Resistance to retort The can which has been good in deep drawing is filled with water and retorted in a steam sterilizer at 120 ° C. for 1 hour.
Stored at 50 ° C. for 30 days. After dropping 10 cans for each test from a height of 50 cm onto a PVC tile floor, an ERV test in the cans was performed. ：: 0.2 mA or less for all 10 samples. C: 0.2 mA or more for 1 to 5 pieces. ×: 0.2 mA or more for 6 or more pieces, or cracks of the film were already observed after dropping.

(11) Preservation of Flavor Retention-1 A can with good deep drawing is filled with ion-exchanged water and stored at room temperature (20 ° C.) for 30 days. A tasting test is carried out by 30 panelists using the immersion liquid, and compared with ion-exchanged water for comparison, and evaluated according to the following criteria. ：: Three or less out of thirty felt changes in taste and aroma as compared with the comparative solution. ：: Four to six out of thirty people felt a change in taste and aroma as compared with the comparative solution. Δ: 7 to 9 out of 30 persons felt a change in taste and aroma as compared with the comparative solution. ×: Ten or more of the 30 persons felt a change in taste and aroma as compared with the comparative solution.

(12) Flavor preservation and flavor retention-2 For cans having good deep drawing, filled with ion-exchanged water, and subjected to a retort treatment at 120 ° C. for 1 hour in a steam sterilizer. C) Store for 30 days. A tasting test is carried out by 30 panelists using the immersion liquid, and compared with ion-exchanged water for comparison, and evaluated according to the following criteria. ：: Three or less out of thirty felt changes in taste and aroma as compared with the comparative solution. ：: Four to six out of thirty people felt a change in taste and aroma as compared with the comparative solution. Δ: 7 to 9 out of 30 persons felt a change in taste and aroma as compared with the comparative solution. ×: Ten or more of the 30 persons felt a change in taste and aroma as compared with the comparative solution.

[Examples 1 to 3, 5 and Comparative Examples 1 and 2] Copolymerized polyethylene terephthalate obtained by copolymerizing the components shown in Table 1 (particles having an intrinsic viscosity of 0.64 and an average primary particle diameter of 0.05 μm) With a pore volume of 1.3m
1 / g, a porous silica particle having an average particle diameter of 0.6 μm was added to 0.1%.
(1% by weight) was dried, melt-extruded, and rapidly solidified to obtain an unstretched film. Next, the unstretched film was longitudinally stretched at the temperature and magnification shown in Table 1, then transversely stretched at the temperature and magnification shown in Table 1, and further heat-set at 180 ° C. to obtain a biaxially stretched polyester film. Below, in the table
“Example 4” is replaced with “Reference Example 1”.

The thickness of each of the obtained films was 25 μm, the surface roughness (Ra) was 0.010 μm, and the thickness of the film was 50 μm.
The number of coarse aggregated particles having a size of m or more was 0 / m ² . Table 2 shows the glass transition temperature (Tg), the peak temperature of the maximum loss modulus (Te), the refractive index in the thickness direction of the film, and the amount of extraction with ion-exchanged water. Table 3 shows the evaluation results.

[0058]

[Table 1]

[0059]

[Table 2]

[0060]

[Table 3]

As is clear from Table 3, in the case of the present invention in which the melting point of the copolyester is 210 to 245 ° C. (Examples 1 to 3, 5), good results were obtained. When the temperature was lower than 210 ° C. (Comparative Example 1), the heat resistance was inferior, the flavor and odor retention after retorting was poor, and when it exceeded 245 ° C. (Comparative Example 2), the moldability was poor.

[Examples 6 and 7 and Comparative Examples 3 and 4] Table 4
(Intrinsic viscosity 0.62, average particle size of primary particles 0.03
It is an aggregate of particles of μm, and has a pore volume of 1.0 ml / g,
0.1% by weight of porous silica particles having an average particle size of 0.8 μm
Was dried and extruded, quenched and solidified, and the unstretched film was stretched and heat-set under the conditions shown in Table 4 to obtain a biaxially stretched polyester film.

The thickness of each of the obtained films was 25 μm. The surface roughness (Ra) was 0.012 μm, and the number of coarse aggregated particles having a size of 50 μm or more in the film was 1 / m ² . Also, the glass transition temperature (T
g), the maximum peak temperature (Te) of the loss elastic modulus, the refractive index in the film thickness direction, and the extraction amount with ion-exchanged water were as shown in Table 5.

The evaluation results are shown in Table 6. In the case of the present invention in which Tg was 78 ° C. or more and Te-Tg was 30 ° C. or less (Examples 6 and 7), good results were obtained. When Tg is less than 78 ° C (Comparative Example 3), heat resistance is inferior, and the flavor and scent retention after retort treatment is poor. When Te-Tg exceeds 30 ° C (Comparative Example 4), moldability is high. Decreased.

[0065]

[Table 4]

[0066]

[Table 5]

[0067]

[Table 6]

Examples 8 to 11 and Comparative Examples 5 to 8 In Example 2, the average primary particle diameter and the pore volume of the porous silica were changed as shown in Table 7, and the biaxially stretched polyester film was obtained. Obtained.

The results are as shown in Table 8, wherein the average particle size of the primary particles of the porous silica is in the range of 0.01 to 0.1 μm and the pore volume is in the range of 0.5 to 2.0 ml / g. In some cases of the present invention (Examples 8 to 11), good results were obtained. However, when the average particle size of the primary particles exceeded 0.1 μm (Example 6) and when the pore volume was 0.5 ml In the case of less than / g (Comparative Example 7), the porosity of the silica was reduced, and the effect of improving the taste and fragrance was small. In addition, when the average particle size of the primary particles is less than 0.001 μm (Comparative Example 5) and when the pore volume exceeds 2.0 ml / g (Comparative Example 8), agglomeration is likely to occur, and pinholes occur during molding. Occurred and the moldability was poor.

[0070]

[Table 7]

[0071]

[Table 8]

[0072]

The polyester film for laminating and processing a metal plate of the present invention is prepared by laminating a metal can with a metal plate after laminating the metal film with a metal plate. While maintaining excellent heat resistance, impact resistance, and retort resistance, the flavor and flavor retention, especially after retort treatment, is improved, and the moldability is not reduced. It is extremely useful as a container film.

Continuation of the front page (51) Int.Cl. ⁷ Identification code FI B29K 67:00 B29K 67:00 B29L 7:00 B29L 7:00 C08L 67:02 C08L 67:02 (56) References JP-A-8-269215 (JP, A) JP-A-7-82391 (JP, A) JP-A-8-92467 (JP, A) JP-A-8-143687 (JP, A) JP-A-9-286866 (JP, A) ( 58) Field surveyed (Int. Cl. ⁷ , DB name) C08J 5/18 B32B 27/36 B32B 15/08

Claims (4)

(57) [Claims] (1) a melting point of 210 to 245 ° C. and a Tg of 78;
Naphthalene dicarboxylic acid at 80 ° C to 83 ° C with total dicarboxylic acid
Copolymerized copolymer obtained by copolymerizing 6 to 18 mol% with respect to the components
A biaxially stretched film made of lentephthalate, the highest peak temperature (Te) of the loss modulus of the film
And a glass transition temperature (Tg) in DSC measurement satisfying the following formulas (1) and (2), and an aggregate of primary particles having an average particle diameter of 0.001 to 0.1 μm, and a pore volume of Containing a porous silica particle having a particle size of 0.5 to 2.0 ml / g. 83 ° C. ≧ Tg ≧ 78 (1) Te−Tg ≦ 30 (2) (Here, Tg is heat-melted at 290 ° C.-DS after quenching.
The glass transition temperature (° C.) and Te in the C measurement are the highest peak temperature (° C.) of the loss modulus of the film. ) 2. The film is treated with ion-exchanged water at 121.degree.
2. The polyester film for laminating and processing a metal plate according to claim 1, wherein the amount of extraction when subjected to the time extraction treatment is 0.5 mg or less per square inch. 3. An average secondary particle diameter of the porous silica particles is as follows:
Polyester film for metal sheet lamination molding according to claim 1 or 2 is 0.1 to 5 [mu] m. 4. The addition amount of the porous silica particles is 0.01 to
The polyester film for lamination processing of a metal plate according to any one of claims 1 to 3 , which is 1% by weight.