WO2015125461A1 - 容器用樹脂被覆金属板およびその製造方法 - Google Patents
容器用樹脂被覆金属板およびその製造方法 Download PDFInfo
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- WO2015125461A1 WO2015125461A1 PCT/JP2015/000719 JP2015000719W WO2015125461A1 WO 2015125461 A1 WO2015125461 A1 WO 2015125461A1 JP 2015000719 W JP2015000719 W JP 2015000719W WO 2015125461 A1 WO2015125461 A1 WO 2015125461A1
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- resin
- resin layer
- polyester
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2309/00—Parameters for the laminating or treatment process; Apparatus details
- B32B2309/02—Temperature
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2311/00—Metals, their alloys or their compounds
- B32B2311/30—Iron, e.g. steel
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/40—Closed containers
- B32B2439/66—Cans, tins
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/04—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the partial melting of at least one layer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/06—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the heating method
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/08—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the cooling method
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/14—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers
- B32B37/16—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with all layers existing as coherent layers before laminating
- B32B37/20—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with all layers existing as coherent layers before laminating involving the assembly of continuous webs only
- B32B37/203—One or more of the layers being plastic
- B32B37/206—Laminating a continuous layer between two continuous plastic layers
Definitions
- the present invention relates to a resin-coated metal plate for containers used in, for example, can bodies and lids for canned foods and a method for producing the same.
- tin free steel which is a material for metal cans used in food cans, and metal plates such as aluminum have been coated for the purpose of improving corrosion resistance, durability, weather resistance, and the like.
- this coating technique has a problem that not only the baking process is complicated, but also a long processing time is required and a large amount of solvent is discharged. Therefore, in order to solve these problems, resin-coated metal plates were developed by laminating thermoplastic resin films on heated metal plates instead of painted metal plates. Widely used.
- Patent Document 1 was filed, assuming that good characteristics could be secured.
- Patent Document 1 it is insufficient to secure good content take-out properties from the strength of the adhesiveness for the content having a high protein content such as luncheon meat and tuna. There was also.
- Patent Document 2 has a high protein content and can secure excellent take-out properties even for highly adherent contents.
- it is necessary to add about 10 to 25 mass% of a low-energy substance having many hydrophobic groups to the resin layer in direct contact with the contents. Since it is necessary to introduce a relatively large amount of additive, the composition of the resin layer is limited, and it is necessarily composed of a plurality of resin layers. Therefore, inconsistency between resin layers is inevitable, and there is room for improvement in adhesion between layers.
- Patent Document 3 is also composed of a plurality of resin layers as in Patent Document 2, and by adding 15 to 20 mass% of fatty acid amide to the uppermost resin layer in contact with the contents, As a result, excellent content takeout property is ensured, and there is room for improvement in adhesion between resin layers.
- An object of the present invention is to provide a resin-coated metal plate for containers and a method for producing the same.
- the present inventors diligently studied to solve the above problems. As a result, paying attention to the resin layer (A) on the inner surface side of the container after forming the container, the uppermost resin layer (a1) in contact with the contents of the resin layer (A). By adding a wax compound to the resin and controlling the crystal structure of the uppermost resin layer (a1), excellent content takeout properties and other required properties (adhesion, moldability, corrosion resistance, etc.) are satisfied. It has been found that a resin-coated metal plate for containers can be obtained.
- the resin layer (A) contains 85 mol% or more of terephthalic acid
- the resin layer (A) is composed of at least two layers, and the uppermost resin layer (a1) in contact with the contents contains 0% of the wax compound with respect to the uppermost resin layer (a1).
- the ratio of the peak intensity (I MD ) in the longitudinal direction to the peak intensity (I ND ) in the thickness direction (I ND ) of the Raman band of 1615 cm ⁇ 1 by Raman spectroscopy with respect to the uppermost resin layer (a1) (I MD / I ND ) is 1.0 or more and 4.0 or less, 4)
- the thickness of the uppermost resin layer (a1) is 0.5 ⁇ m or more and 10 ⁇ m or less, 5)
- the resin-coated metal sheet for containers according to [1] or [2] above which contains the following components (I) to (V): (I) Polyester resin (II) Phenol resin (III) Metal alkoxide compound and / or metal chelate compound (IV) Epoxy resin (V) One or more selected from the group consisting of polyamine resin, polyamidoamine resin, and polyamide resin [4]
- the resin layer (B) includes the resin layer (b1) and the resin layer (b1).
- Polyester resin 50-89 mass%
- Phenolic resin 10 to 45 mass%
- Metal alkoxide compound and / or metal chelate compound 0.01 to 10 mass%
- Epoxy resin 0.5 to 20 mass%
- the resin in the resin layer (b2) contains a polyester (i) composed of polyethylene terephthalate or a copolymerized polyethylene terephthalate having a copolymerization component content of less than 6 mol%, and a polybutylene terephthalate or copolymer component.
- the resin layer (B), the resin layer (b1) and the uppermost resin layer (b2) excluding the uppermost layer, or the uppermost resin layer (b2) contains a wax compound
- the present invention it is possible to obtain a resin-coated metal plate for containers having excellent take-out properties for various contents. Moreover, the resin-coated metal plate for containers of the present invention can stably satisfy many characteristics required for food canning materials.
- FIG. 1 is a view showing a main part of a laminating apparatus for a metal plate.
- FIG. 2 is a diagram showing a cross-sectional structure of a resin-coated metal plate for containers.
- FIG. 3 is a diagram illustrating a position of a cross cut wound applied to the can body portion.
- FIG. 4 is a diagram showing a method for measuring the maximum corrosion width from an artificial wound. (Example 1)
- the resin-coated metal plate for containers of the present invention will be described in detail.
- the metal plate used by this invention an aluminum plate or a mild steel plate widely used as a can material can be used.
- a surface-treated steel sheet (so-called TFS) in which a two-layer film having a lower layer composed of metallic chromium and an upper layer composed of chromium hydroxide is formed is optimal.
- the amount of adhesion of the metal chromium layer and chromium hydroxide layer of TFS is not particularly limited, but from the viewpoint of adhesion after processing and corrosion resistance, both are in terms of Cr, the metal chromium layer is 70 to 200 mg / m 2 , chromium The hydroxide layer is desirably in the range of 10 to 30 mg / m 2 .
- composition of resin layer (A) on inner surface of container it has the resin layer (A) of the multilayer structure which has polyester as a main component on the side used as the container inner surface when shape
- This resin layer (A) is a polymer composed of a dicarboxylic acid component and a glycol component, and is characterized by containing 85 mol% or more of terephthalic acid as the dicarboxylic acid component.
- terephthalic acid is less than 85 mol%, the melting point of the resin is lowered, and the resin is softened by frictional heat at the time of molding the container, which may cause damage such as film scraping.
- the resin layer is attacked by water vapor and the adhesion in a wet environment is deteriorated.
- Dicarboxylic acid components other than terephthalic acid include aromatic dicarboxylic acids such as isophthalic acid, naphthalenedicarboxylic acid, diphenyldicarboxylic acid, 5-sodium sulfoisophthalic acid, phthalic acid, oxalic acid, succinic acid, adipic acid, sebacic acid, dimer Examples thereof include aliphatic dicarboxylic acids such as acid, maleic acid and fumaric acid, alicyclic dicarboxylic acids such as cyclohexanedicarboxylic acid, and oxycarboxylic acids such as p-oxybenzoic acid.
- aromatic dicarboxylic acids such as isophthalic acid, naphthalenedicarboxylic acid, diphenyldicarboxylic acid, 5-sodium sulfoisophthalic acid, phthalic acid, oxalic acid, succinic acid, adipic acid, sebacic acid, dim
- glycol component examples include aliphatic glycols such as ethylene glycol, propanediol, butanediol, pentanediol, hexanediol, and neopentylglycol, alicyclic glycols such as cyclohexanedimethanol, and aromatics such as bisphenol A and bisphenol S. Glycol and the like.
- aliphatic glycols such as ethylene glycol, propanediol, butanediol, pentanediol, hexanediol, and neopentylglycol
- alicyclic glycols such as cyclohexanedimethanol
- aromatics such as bisphenol A and bisphenol S. Glycol and the like.
- ethylene glycol is preferable among these glycol components.
- dicarboxylic acid components and glycol components may be used in combination of two or more.
- the resin layer (A) is composed of at least two layers, and the uppermost resin layer (a1) in contact with the contents contains a wax compound as the uppermost resin layer (a1).
- the wax compound is characterized by containing 0.10 to 2.0 mass%.
- the purpose of adding the wax compound is to reduce the surface free energy of the resin layer (A). By adding the wax compound, it becomes difficult for the contents to adhere to the resin layer (A), and the contents can be taken out easily. improves.
- the reason for limiting to 0.10 mass% or more is that when the content is less than 0.10 mass%, the above-described effect becomes poor, and the contents can be easily taken out.
- the reason for limiting to 2.0 mass% or less is that if it exceeds 2.0 mass%, it becomes a difficult region in terms of film deposition technology, resulting in poor productivity and high cost.
- the presence or absence of the wax addition to the resin layers other than the uppermost layer is not particularly limited, even when added, it is preferably set to 2.0 mass% or less.
- a wax compound is added to a resin layer other than the uppermost layer, the effect of improving the contents take-out property may not be seen, so it is effective to add it only to the uppermost layer.
- An organic / inorganic lubricant can be used as a component of the wax compound to be added.
- carnauba wax which is one of vegetable waxes and is a natural wax, is preferable.
- the polyester resin containing carnauba wax can be produced by a usual production method after blending a predetermined amount of wax with polyester.
- the uppermost resin layer (a1) is longer than the uppermost resin layer (a1) in the longitudinal direction (surface of the resin layer (a1)) with respect to a 1615 cm ⁇ 1 Raman band (I 1615 ) by Raman spectroscopy.
- the maximum value of the ratio (I MD / I ND ) of the peak intensity (I MD ) in the direction parallel to the surface and the peak intensity (I ND ) in the thickness direction (direction perpendicular to the surface of the resin layer (a1)) It is 0 or more and 4.0 or less.
- the Raman band of I 1615 tends to increase in peak intensity when the polyester molecular chains are aligned with each other and the degree of orientation increases. Therefore, when the peak intensity ratio (I MD / I ND ) of the Raman band is increased, the polyester molecular chain is more strongly oriented with respect to the surface direction of the resin layer (a1). On the other hand, when the peak intensity ratio (I MD / I ND ) of the Raman band is reduced, the degree of orientation of the polyester molecular chain relative to the surface direction of the resin layer (a1) is also reduced.
- the crystal lattice of a wax compound such as carnauba wax added in the resin layer (a1) is the distance between the molecular chains when the molecular chains of the polyester that is the main component of the resin layer (a1) form an oriented structure. Therefore, it cannot exist in the alignment structure. Therefore, the wax compound exists only in the non-oriented structure of the polyester molecular chain.
- the polyester resin constituting the resin layer (a1) has a glass transition temperature (Tg) (° C.) of about 70 ° C. Below this temperature, the movement of the molecular chain is frozen, so that the wax compound is also in the non-oriented structure. It is fixed.
- the structure of the resin layer (a1) is stable, and the wax compound remains in the non-oriented structure in the resin layer (a1).
- the molecular chain constituting the non-oriented structure of the polyester resin starts micro-Brownian motion. Move inside. Since the wax compound has lower surface free energy than the polyester resin, it diffuses and concentrates on the surface of the resin layer (a1). Thereby, the surface free energy of the resin layer (a1) is lowered, and the contents can be easily taken out.
- the content takeout property is improved.
- the polyester molecular chain arranged in this way also has a function as a barrier layer for water vapor causing retort whitening, chlorine ions, water, oxygen, etc. causing corrosion. Therefore, it is necessary to control the degree of orientation of the polyester molecular chain in the surface direction of the film within a range that balances the required characteristics.
- the Raman band of 1615 cm -1 by Raman spectroscopy, the maximum value of the ratio (I MD / I ND) in the longitudinal direction of the peak intensity (I MD) and the thickness direction of peak intensity (I ND) is 1. 0 or more and 4.0 or less.
- the surface concentration of the wax compound becomes smooth, excellent contents can be taken out, and sufficient barrier properties against water vapor and corrosion factors can be secured.
- the maximum value of the peak intensity ratio ( IMD / IND ) is less than 1.0, the degree of orientation is insufficient, resulting in a decrease in barrier properties, which may cause retort whitening and corrosion resistance deterioration.
- the degree of orientation becomes excessive, and the surface concentration of the wax compound is inhibited, so that sufficient content takeout properties cannot be obtained.
- the thickness of the resin layer (a1) is in the range of 0.5 ⁇ m to 10 ⁇ m. Since the addition amount of the wax compound is limited to 2.0 mass% or less with respect to the resin layer (a1), when the thickness of the resin layer (a1) is less than 0.5 ⁇ m, the wax content itself is insufficient. , Sufficient contents take-out property cannot be obtained. On the other hand, if it exceeds 10 ⁇ m, the ratio of the resin layer (a1) to the resin layer (A) becomes excessive, and the adhesion between the resin layer (A) and the metal plate, the moldability of the resin layer (A), the corrosion resistance, etc. There is a concern that the function will be reduced.
- the thickness of the resin layer (a1) is 0.5 ⁇ m or more and 10 ⁇ m or less.
- the thickness of the resin layer (A) excluding the thickness of the uppermost resin layer (a1) is 5 ⁇ m or more and 20 ⁇ m or less.
- the resin layer (a2) ensures adhesion to the metal plate. The resin strength sufficient to maintain the interfacial adhesion with the resin layer (a1) cannot be maintained.
- the thickness of the resin layer (A) excluding the thickness of the uppermost resin layer (a1), that is, the thickness of the resin layer (a2) is 5 ⁇ m or more and 20 ⁇ m or less.
- composition of resin layer (B) on outer surface side of container When the metal plate is formed into a container, the resin layer (B1) having a multilayer structure composed mainly of polyester on the side that becomes the outer surface of the container, and the resin layer (b1) in contact with the metal plate has the following (I ) To (V) are preferably contained.
- Polyester resin (I) Phenol resin (III) Metal alkoxide compound and / or metal chelate compound (IV) Epoxy resin (V) One or more selected from the group consisting of polyamine resin, polyamidoamine resin, polyamide resin
- the resin layer (B) is mainly composed of a polyester resin, where the main component is a resin coating layer ( The resin component in B) contains 50% by mass or more of a polyester resin.
- polyester resin preferably has a number average molecular weight of 3,000 to 100,000, more preferably 5,000 to 30,000, and still more preferably 10,000 to 25,000.
- the number average molecular weight is a conversion value by comparison with polystyrene in gel permeation chromatography analysis. If the number average molecular weight is lower than 3000, the processability is deteriorated, and if it is higher than 100,000, the viscosity at the time of coating may be increased and appropriate coating may not be performed.
- the glass transition temperature of the polyester resin is preferably in the range of 0 ° C. or more and less than 100 ° C. By setting the glass transition temperature in the range of 0 ° C.
- the flexibility, workability, and blocking resistance of the resin are appropriately balanced and suitable for food canning applications.
- polyester resin it may be difficult to satisfy many required performances.
- the glass transition temperature of the polyester resin is 0 ° C. or higher and lower than 35 ° C.
- flexibility is imparted to the resin layer, so that workability is excellent.
- the film may be blocked.
- the retort resistance is slightly inferior.
- the glass transition temperature is 35 ° C.
- the film does not block and the aesthetic appearance of the film is not impaired.
- the glass transition temperature is 65 ° C. or more and less than 100 ° C., although the blocking property is excellent, the film becomes hard and the workability is somewhat inferior. Therefore, it is preferable to obtain a balanced and more excellent resin layer by using a plurality of resins having different glass transition temperatures in combination with the polyester resin to bring out the good performance of each polyester resin.
- the ratio of each polyester resin has the following preferable.
- the polyester resin preferably contains a repeating unit derived from diphenolic acid.
- diphenol acid is contained in the monomer composition which is a raw material component for producing the polyester resin, the reactivity with the phenol resin is increased and the curing rate is increased, and as a result, the resistance to retort whitening is improved. Further, even when a polyester having a glass transition temperature of 0 ° C. or more and less than 35 ° C. using diphenol acid as an essential monomer is used in a high ratio, the curability is improved.
- the polyester resin preferably contains a repeating unit derived from diphenolic acid because it has a feature such that the blocking property of the coating film is excellent even when the glass transition temperature is low.
- polyester resin (I) what made the esterification reaction of a polybasic acid component and a polyhydric alcohol component can be used.
- the polybasic acid component include one or more dibasic acids such as phthalic anhydride, isophthalic acid, terephthalic acid, succinic acid, fumaric acid, adipic acid, azelaic acid, sebacic acid, dimer acid, and the like.
- Lower alkyl esterified products are used, and monobasic acids such as benzoic acid and crotonic acid, tribasic or higher polybasic acids such as trimellitic anhydride and methylcyclohexytricarboxylic acid are used in combination as necessary.
- polyhydric alcohol component examples include ethylene glycol, diethylene glycol, propylene glycol, 1,4 butanediol, neopentyl glycol, 3-methylpentanediol, 1,4-hexanediol, 1,6-hexanediol, and cyclohexanedimethanol.
- a dihydric alcohol is mainly used, and a trihydric or higher polyhydric alcohol such as glycerin, trimethylolethane, trimethylolpropane, pentaerythritol can be used in combination as necessary.
- These polyhydric alcohols can be used alone or in admixture of two or more.
- polyester resin (I) examples include Byron 300, 500, 560, 600, 630, 650, 670, Byron GK130, 140, 150, 190, 330, 590, 680, manufactured by Toyobo Co., Ltd. 780, 810, 890, Elitel UE-3220, 3500, 3210, 3215, 3216, 3620, 3240, 3250, 3300 manufactured by Unitika Ltd., Aronmelt PES-310, 318, 334 manufactured by Toagosei Co., Ltd. .
- a phenol resin as component (II) it is preferable to add a phenol resin as component (II) to the phenol resin resin layer (b1). By adding a phenol resin, a cross-linking reaction occurs and a three-dimensional network structure is formed, so that the effect of improving the corrosion resistance and retort resistance of the film can be obtained.
- Trifunctional phenolic compounds such as carboxylic acid, m-cresol, m-ethylphenol, 3,5-xylenol, m-methoxyphenol, or p-cresol, o-cresol, p-tert-butylphenol, p-ethylphenol, Examples thereof include those obtained by synthesizing various bifunctional phenols such as 2,3-xylenol, 2,5-xylenol, m-methoxyphenol, and formaldehyde in the presence of an alkali catalyst. These phenol compounds can be used alone or in combination of two or more. Further, it is possible to use a form in which some or all of the methylol groups contained in the phenol resin are etherified with alcohols having 1 to 12 carbon atoms.
- (III) Metal alkoxide compound and / or metal chelate compound The metal alkoxide compound and / or metal chelate compound react with (I) polyester resin, (II) phenol resin, and (IV) epoxy resin.
- a crosslinking reaction proceeds between the functional group of each resin and the metal alkoxide compound and / or metal chelate compound.
- This cross-linking reaction has an extremely fast curing rate compared to the case where there is no metal alkoxide compound and / or metal chelate compound, and as a result, excellent adhesion, workability, Retort and corrosion resistance can be expressed. For example, existing laminated cans are baked at 180 ° C.
- the post-heating is used to cure the resin film to ensure the above various required performances.
- the resin layer containing a metal alkoxide compound and / or a metal chelate compound is sufficiently cured only by heating for a short time of about 1 second when performing heat fusion lamination.
- the performance equal to or better than that after post-heating can be obtained. Therefore, the post-heating step in the manufacturing process is not necessary, and the manufacturing efficiency is greatly improved.
- carbon dioxide emissions can be reduced, which can be a very useful technique in practice.
- the strength of the film is improved, and as a result, impact resistance and corrosion resistance are greatly improved.
- the resin layer (b1) preferably contains a metal alkoxide compound and / or a metal chelate compound.
- the metal alkoxide compound and / or metal chelate compound include alkoxide metal compounds such as aluminum, titanium, tin, and zirconium, and metal chelate compounds in which acetoacetic acid is coordinated to the metal.
- a metal alkoxide compound and / or a metal chelate compound and a polyester resin and / or a phenol resin continuously undergo a crosslinking reaction, whereby a three-dimensional network of molecular chains is formed in the resin layer.
- Discoloration due to water vapor is a phenomenon in which the resin layer itself is discolored so as to become cloudy during retort sterilization, and is called retort whitening. This is a major problem that can reduce the consumer's willingness to purchase since it impairs the design of the outer surface of the can.
- the water vapor diffusing in the resin is cooled as it approaches the metal plate, and liquefies at the interface with the metal plate and in the vicinity of the interface to form condensed water and form a vacuole.
- the vacuole remains at the interface and in the vicinity of the interface even after the retort treatment, which causes light scattering and makes the resin surface appear cloudy. Therefore, in order to suppress retort whitening, the formation of vacuoles at the interface with the metal plate and in the vicinity of the interface may be suppressed.
- the retort processing apparatus there is a retort processing apparatus that uses hot water as a heating medium in addition to the apparatus that uses water vapor as a heating medium as described above.
- a retort processing apparatus using hot water as a heating medium there arises a problem that the resin layer itself is discolored and the design properties are deteriorated by a mechanism different from discoloration due to water vapor.
- the water that has penetrated into the resin layer promotes the hydrolysis reaction of the polyester molecular chain using the carbonyl terminal group of the polyester as a catalyst. It is believed that large vacuoles are formed in the resin layer.
- the network of polyester molecular chains prevents water vapor and hot water from penetrating into the resin and reaching the interface, and it is thought that the formation and growth of vacuoles can be suppressed by increasing the resin strength and elastic modulus. It is done. Moreover, a rapid hydrolysis reaction is also suppressed by the decrease in the amount of carbonyl end groups accompanying the formation of a molecular chain network. Therefore, the metal alkoxide compound and / or the metal chelate compound is preferably a titanium alkoxide compound and / or a titanium chelate compound.
- Epoxy resin The epoxy resin mainly improves the adhesion of the film.
- a novolac type epoxy resin is preferable.
- DIC Corporation Epicron N-665, 670, 673, 680, 690, 695, 730, 740, 770, 865, 870, XD-manufactured by Dow Chemical Co., Ltd. 7855, ECN-1273, 1299 manufactured by Asahi Kasei Epoxy Corporation.
- Examples of the biphenyl type epoxy resin include YL6121H and YX7399 manufactured by Mitsubishi Chemical Corporation.
- the epoxy resin is preferably other than bisphenol A. This is because bisphenol A is concerned about endocrine disrupting effects.
- polyamine resins, polyamidoamine resins, and polyamide resins selected from the group consisting of polyamine resins, polyamidoamine resins, and polyamide resins have a faster curing speed and can form a tough film compared to melamine resins, etc. Is excellent. Compared with resin compositions composed of polyester / melamine, epoxy / melamine, etc., it has excellent curing characteristics, so it can exhibit particularly excellent performance in terms of retort resistance, corrosion resistance and workability of laminated steel sheets. It becomes possible.
- polyamine resin examples include diethylenetriamine, triethylenetriamine, triethylenepentamine as the aliphatic amine, and isophoronediamine as the alicyclic polyamine.
- an epoxy resin or acrylonitrile may be added to an aliphatic polyamine or modified by reacting formaldehyde and phenol to improve workability, reduce irritation, or improve mechanical properties.
- aromatic polyamine examples include metaphenylenediamine, diaminodiphenylsulfonic acid, and diaminodiphenylmethane.
- commercially available products include EPICRON EXB-353 manufactured by DIC Corporation, Ancamine 2596 manufactured by Air Products Japan Co., Ltd., and Ancamine 2605.
- Polyamide amine resin and polyamide resin are compounds synthesized by, for example, dehydration condensation reaction between fat and fatty acid and polyamine.
- Examples of commercially available products include Polyamide L-15-3, Polyamide L-45-3 manufactured by Sanyo Chemical Co., Ltd., Ancamide 2137 manufactured by Air Products Japan Co., Ltd., Sunmide 330, Sunmide X-2000, and the like.
- the ratio of the resin component forming the resin layer (b1) preferably satisfies the following.
- Polyester resin 50-89 mass%
- Phenolic resin 10 to 45 mass%
- Metal alkoxide compound and / or metal chelate compound 0.01 to 10 mass%
- Epoxy resin 0.5 to 20 mass%
- the ratio of the polyester resin is lower than 50 mass%, the workability deteriorates, and when it exceeds 89 mass%, the curability is insufficient and the retort resistance may be lowered.
- the ratio of the phenol resin is lower than 10 mass%, the curability is insufficient and the retort resistance is inferior, and when it exceeds 45 mass%, the workability may be deteriorated. More preferably, it is 20 to 40 mass%.
- the thickness (average film thickness) of the resin layer (b1) is preferably specified in the range of 0.1 ⁇ m to 5.0 ⁇ m. If it is less than 0.1 ⁇ m, the surface of the metal plate cannot be uniformly coated, and the film thickness may be non-uniform. On the other hand, if it exceeds 5.0 ⁇ m, the cohesive force of the resin becomes insufficient, and the strength of the resin layer may be reduced. As a result, at the time of can manufacturing, the resin layer is agglomerated and broken, and the film is peeled off, and the can body portion is torn from there.
- the film thickness (average film thickness) is preferably from 0.1 ⁇ m to 5.0 ⁇ m, more preferably from 0.1 ⁇ m to 3.0 ⁇ m, and even more preferably from 0.5 ⁇ m to 2.5 ⁇ m.
- the adhesion amount of the resin layer (b1) can be converted from the film thickness by the specific gravity of the film component. However, in the case of the composition of the present invention, there is no problem even if the specific gravity is converted to approximately 1.
- Colorant of resin layer (b1) By adding colorants such as dyes and pigments to the resin layer (b1), the underlying metal plate can be concealed and various colors unique to the resin can be imparted. For example, by adding carbon black as a black pigment, it is possible to conceal the metal color of the base and to impart a high-class feeling of black to food cans.
- the particle size of carbon black can be in the range of 5 to 50 nm. Among these, the range of 5 to 30 nm is preferable in consideration of dispersibility and color developability in the polyester resin.
- the black pigment by adding a white pigment, the metallic luster of the base can be concealed, the printed surface can be sharpened, and a good appearance can be obtained.
- an inorganic pigment such as titanium dioxide can be used. Since the coloring power is strong and rich in spreadability, it is preferable because a good design property can be secured even after container molding.
- a yellow organic pigment If a bright color is desired on the container surface, it is preferable to use a yellow organic pigment. Although it is excellent in transparency, it has a strong coloring power and a high spreadability, so that a bright appearance can be obtained even after the container is molded.
- organic pigments that can be used in the present invention include a color index (abbreviation: CI) of Pigment Yellow 12, 13, 14, 16, 17, 55, 81, 83, 139, 180, 181, 183. 191 and 214.
- C.I. I. Pigment Yellow 180 and 214 are more preferably used.
- the blending ratio of the above colorants is preferably 0.1 to 70 PHR with respect to the amount of resin in the resin layer (b1).
- a curing catalyst that promotes crosslinking can be added to the resin layer (b1).
- inorganic acids such as phosphoric acid
- organic acids such as dodecylbenzenesulfonic acid and toluenesulfonic acid, and those blocked with an amine or the like can be used.
- the blending ratio of the curing catalyst is preferably 0.01 to 5 PHR with respect to the amount of resin in the resin layer (b1).
- lubricants such as a melamine resin, a benzoguanamine resin, and an isocyanate resin can be used in combination as a curing auxiliary agent, and these can be used in combination with an appropriate one depending on the drying conditions and lamination conditions of the film.
- the resin layer (b2) formed on the upper layer of the resin layer (b1) will be described.
- polyester film (b2) As a composition of the polyester film (b2), polyethylene terephthalate or copolymerized polyethylene terephthalate (hereinafter sometimes referred to as polyester (i)) having a copolymer component content of less than 6 mol% and polybutylene terephthalate (hereinafter referred to as “polyethylene terephthalate”). It is preferable that the ratio of polyester (i) is 60 mass% or less and the ratio of polyester (ii) is 40 mass% or more.
- the ratio of polyester (ii) is less than 40 mass%, condensation of water vapor during retort sterilization treatment cannot be suppressed, and vacuoles may be formed in the resin layer. This may remain in the resin layer even after the retort sterilization treatment, thereby causing scattering of visible light, changing the appearance of the resin and reducing the design.
- the ratio of polyester (i) is larger than 60 mass%, resin discoloration during the retort sterilization treatment can be suppressed, but the heat resistance and mechanical properties of the resin tend to deteriorate, and stress and friction during can processing There is a concern that the resin may be damaged by the influence of heat or the like.
- polyester (i) since Tg of polyester (i) is about 40 ° C., which is lower than that of polyester (ii), the corrosion resistance is greatly deteriorated when the barrier property of the resin is greatly lowered when exposed to a temperature exceeding normal temperature. There are concerns. For this reason, the ratio of polyester (i) is preferably in the range of 40 mass to 60 mass%. More preferably, it is in the range of 45 to 58 mass%, still more preferably 50 to 56 mass%. In addition, polyester (i) may contain a copolymerization component in the range below 6 mol% as a range which does not impair the effect of invention. The copolymer component may be an acid component or an alcohol component.
- the acid component includes aromatic dicarboxylic acids such as isophthalic acid, phthalic acid and naphthalenedicarboxylic acid, aliphatic dicarboxylic acids such as adipic acid, azelaic acid, sebacic acid and decanedicarboxylic acid, and alicyclic such as cyclohexanedicarboxylic acid.
- aromatic dicarboxylic acids such as isophthalic acid, phthalic acid and naphthalenedicarboxylic acid
- aliphatic dicarboxylic acids such as adipic acid, azelaic acid, sebacic acid and decanedicarboxylic acid
- alicyclic such as cyclohexanedicarboxylic acid.
- dicarboxylic acid isophthalic acid is most preferred from the viewpoint of moldability.
- the alcohol component examples include aliphatic diols such as diethylene glycol, propanediol, butanediol, and hexanediol, and alicyclic diols such as cyclohexanedimethanol.
- Polyester (ii) is a polycondensation containing a terephthalic acid component and a 1,4-butanediol component as main components, but the other components are contained within a range of less than 5 mol% as long as the effects of the present invention are not impaired. It may be copolymerized.
- the copolymer component may be an acid component or an alcohol component.
- Copolymeric acid components include aromatic dicarboxylic acids such as isophthalic acid, phthalic acid and naphthalenedicarboxylic acid, aliphatic dicarboxylic acids such as adipic acid, azelaic acid, sebacic acid and decanedicarboxylic acid, and alicyclic dicarboxylic acids such as cyclohexanedicarboxylic acid.
- aromatic dicarboxylic acids such as isophthalic acid, phthalic acid and naphthalenedicarboxylic acid
- aliphatic dicarboxylic acids such as adipic acid, azelaic acid, sebacic acid and decanedicarboxylic acid
- alicyclic dicarboxylic acids such as cyclohexanedicarboxylic acid.
- An acid etc. can be illustrated. Of these, isophthalic acid, 2,6-naphthalenedicarboxylic acid or adipic acid is preferred.
- copolymerized alcohol component examples include aliphatic diols such as ethylene glycol, propanediol, and hexanediol, and alicyclic diols such as cyclohexanedimethanol. These can be used alone or in combination of two or more.
- Wax compound Furthermore, in this invention, in order to prevent the damage
- the film formability of the resin layer (B) becomes difficult, it is not preferable.
- the content of the wax compound is less than 0.02 mass%, the effect of preventing wrinkling and scraping of the resin layer (B) due to the addition of the wax compound may not be obtained. 0.02 mass% or more is preferable.
- the wax compound can be contained in both or either of the uppermost resin layer (b2) and the resin layer (b1) excluding the uppermost layer. Among them, the wax compound should be contained in the uppermost resin layer (b2) in order to prevent scratches and scraping of the resin layer (B) during high processing and to ensure moldability during high processing. Is preferred. Further, when the wax compound is contained only in the uppermost resin layer (b2), the content of the wax compound for obtaining the effect is less than that in the resin layer (B) as a whole. be able to.
- the content of the wax compound in the uppermost resin layer (b2) is relative to the resin layer (B) (when converted to the entire layer).
- 5.0 mass% or less is preferable, and the content of the uppermost resin layer (b2) is also preferably 5.0 mass% or less. If the content exceeds 5.0 mass%, the adhesiveness between the resin layer (B) and the ink deteriorates when printing or printing on the outer surface of the container, which is not preferable for printing applications. Moreover, since the film formability of the resin layer (B) becomes difficult, it is not preferable.
- the lower limit of the content of the wax compound in the uppermost resin layer (b2) is 0. With respect to the resin layer (B) (when converted to all layers) in order to obtain the effect of containing the wax compound. It is preferable to set it to 02 mass%.
- the upper limit of the content of the wax compound in each of the content of the entire resin layer (B), the content of the uppermost resin layer (b2), and the content of the resin layer (b1) excluding the uppermost layer is 5. It is preferable to set it to 0.0 mass%.
- the amount of the wax compound in terms of the total resin layer (B) is the uppermost resin layer (b2) and the resin layer (b1) excluding the uppermost layer when the wax is also included. It can be determined by dividing the mass of the wax compound contained in the resin layer (b1) excluding b2) and the uppermost layer by the mass of the entire resin layer (B).
- the wax compound is not particularly limited. Either an organic lubricant or an inorganic lubricant can be used.
- the wax component similar to the resin layer (A) can be used.
- a wax compound having a high melting point is preferred because the outer surface side of the container tends to have a higher temperature on the resin surface due to friction with the mold than the inner surface during can processing.
- the melting point of the wax compound is preferably 50 ° C. or higher, more preferably 70 ° C. or higher.
- Preferred wax compounds are natural waxes such as carnauba wax and candelilla wax, fatty acid esters such as stearic acid esters, polyolefin waxes such as polyethylene wax, and the like. These wax compounds can be used alone or in combination of two or more.
- the manufacturing method of the resin-coated metal plate for containers of the present invention will be described.
- covers a metal plate is demonstrated.
- the method for producing the resin layers (A) and (B) For example, after drying each polyester resin as necessary, the film components are supplied to a known melt lamination extruder, extruded from a slit-shaped die into a sheet, and brought into close contact with the casting drum by a method such as electrostatic application. Cool and solidify to obtain an unstretched film (sheet).
- an objective film component is introduced into a lamination extruder to obtain an unstretched film having a multilayer structure.
- a biaxially stretched film is obtained by stretching this unstretched film in the longitudinal direction and the width direction.
- the draw ratio can be arbitrarily set according to the orientation degree, strength, elastic modulus and the like of the target film.
- a tenter method is preferred in terms of film quality.
- a sequential biaxial stretching method of stretching in the width direction after stretching in the longitudinal direction and a simultaneous biaxial stretching method of stretching in the longitudinal direction and the width direction almost the same are preferable.
- the formation method of the multilayer structure of the resin layer is not particularly limited, but as an example, the resin layer (b1) is formed on the surface of the polyester film (b2).
- the method of forming is described below.
- a polyester resin as a main component is dissolved in an organic solvent, and an additive component and an optional additive component of the resin layer (b1) defined by the present invention are dissolved or dispersed in an organic solvent to prepare a coating liquid.
- the coating liquid is applied to the film surface during or after the formation of the polyester film (b2) and dried to form the resin layer (b1).
- organic solvent for dissolving the polyester resin examples include aromatic hydrocarbon solvents such as toluene and xylene, ketone solvents such as methyl ethyl ketone and cyclohexanone, and ester solvents such as ethyl acetate and ethylene glycol monoethyl ether acetate. One or more of these can be selected and used as appropriate.
- lubricants such as a melamine resin, a benzoguanamine resin, and an isocyanate resin may be used in combination as a curing auxiliary agent, and these can be used in combination with an appropriate one depending on the drying conditions and lamination conditions of the film.
- additives such as carbon black and azo pigments as a crosslinking agent, a curing catalyst, and a colorant specified in the present invention can be dispersed in an organic solvent.
- a dispersant it is preferable to use a dispersant in combination because the uniformity of the additive can be imparted.
- known coating means such as a roll coater method, a die coater method, a gravure method, a gravure offset method, and a spray coating method can be applied.
- the gravure roll coating method is most suitable.
- the drying conditions after applying the coating solution are preferably 80 to 180 ° C. for 1 to 30 seconds, particularly 150 to 170 ° C. for 5 to 30 seconds.
- the thickness of the resin layer (b1) after drying is preferably in the range of 0.1 to 5.0 ⁇ m.
- the thickness is in the range of 0.1 to 5.0 ⁇ m, the continuous uniform coating property is excellent, there is no problem in design, retort resistance and adhesion can be secured, and the blocking property at the time of film winding is also eliminated.
- the thickness is less than 0.1 ⁇ m, it is easy to cause difficulty in the continuity of the film, and it may be difficult to express physical properties and design properties.
- steam is inferior in a retort sterilization process, a water
- a more preferable range is 0.5 to 2.5 ⁇ m.
- a method for producing a resin-coated metal plate by laminating a resin layer (film) on a metal plate will be described.
- a laminate roll a pressure-bonding roll
- the lamination conditions are appropriately set so that the resin layer specified in the present invention is obtained.
- the surface temperature of the metal plate at the start of lamination needs to be equal to or higher than the Tm (melting point) (° C.) of the resin layer in contact with the metal plate. Specifically, it is necessary to control the temperature within the range of Tm to Tm + 40 ° C. of the resin layer.
- the resin layer melts and wets the surface of the metal plate, and good adhesion to the metal plate can be ensured.
- Tm + 40 ° C. the resin layer is excessively melted and the resin layer may adhere to the laminate roll, and the crystal structure of the surface resin layer (a1) is controlled within the specified range of the present invention. It becomes difficult. Tm to Tm + 25 ° C. is preferable, and Tm to Tm + 15 ° C. is more preferable.
- the crystal structure of the resin layer (a1) which is the uppermost layer of the resin layer (A)
- adjustment of the contact time with the laminate roll is also an important factor.
- the contact time needs to be controlled in the range of 10 to 15 msec.
- the crystal structure of the resin layer (a1) defined by the present invention can be realized by adjusting the surface temperature of the laminate roll and the contact time within the above ranges.
- the resin layers (A) and (B) it is preferable to heat the resin layers (A) and (B) before further laminating.
- the temperature distribution in the cross section of the resin layer at the time of lamination can be made more uniform.
- the crystal structure in the cross section of the resin layer also exhibits a more uniform performance since the structural change from the interface with the metal plate to the surface layer becomes gradual.
- the time until quenching is preferably within 5 seconds, and the water temperature of quenching needs to be Tg or less.
- the resin layer is preferably formed into a film and coated on a metal plate.
- the crystal structure defined in the present invention may not be achieved.
- each polyester resin shown in Tables 3 and 4 phenol resin, metal alkoxide compound and / or metal chelate compound, epoxy resin, polyamine resin, polyamidoamine resin, polyamide resin and colorant, the ratio shown in Tables 3 and 4 was dissolved in a mixed solvent of toluene and methyl ethyl ketone to prepare a coating solution.
- a synthesis example of a polyester resin (I-1) containing a repeating unit derived from diphenolic acid is shown.
- an acid component 50 parts by mass of terephthalic acid, 112 parts by mass of isophthalic acid, 4.9 parts by mass of diphenolic acid, and 50 parts by mass of 2-ethyl-2-butyl-1,3-butanediol as a polyhydric alcohol component, , 99 parts by mass of 4-butanediol, 48 parts by mass of 1,4-cyclohexanedimethanol and 0.07 parts by mass of titanium tetrabutoxide were charged into a 2 L flask, and the temperature was gradually raised to 220 ° C. over 4 hours. Esterification was carried out.
- the polymerization was carried out under reduced pressure up to 10 mmHg over 30 minutes, the temperature was raised to 250 ° C., and the latter polymerization was carried out at 1 mmHg or less for 50 minutes.
- the polymerization under reduced pressure was stopped, the mixture was cooled to 220 ° C. under a nitrogen stream, 1.9 parts by mass of trimellitic anhydride was added, and the mixture was stirred at 220 ° C. for 30 minutes to perform carboxy group modification (post-addition), and then resin
- the polyester resin (I-1) having a number average molecular weight of 22,000, an acid value of 5 (mgKOH / g) and a glass transition temperature of 30 ° C. was obtained.
- Byron GK-640 number average molecular weight: 18000, glass transition temperature: 79 ° C., manufactured by Toyobo Co., Ltd.
- TD2495 paracresol type phenol resin, 50% normal butanol solution, manufactured by DIC Corporation, which is a commercial product, was used.
- metal chelate compound (III) commercially available TC-200 (titanium octylene glycol chelate, manufactured by Matsumoto Fine Chemical Co., Ltd.) or the like is used.
- metal alkoxide compound (c) commercially available ZA-65 (zirconium butoxide, Matsumoto Fine Chemical Co., Ltd.) was used.
- epoxy resin (IV) commercially available epiclone N-660 (cresol novolac type epoxy resin, 50% methyl ethyl ketone solution, manufactured by DIC Corporation) and commercially available YL6121H (biphenyl type epoxy resin, manufactured by Mitsubishi Chemical Corporation) was used.
- polyamine resin (V) a commercially available product EPICRON EXB-353 (manufactured by DIC Corporation) was used.
- a commercially available SUNMIDE 328A (manufactured by Air Products Japan Co., Ltd.) was used as the polyamide amine resin.
- polyamide resin commercially available polyamide L-15-3, manufactured by Sanyo Kasei Co., Ltd. was used.
- the coating liquid is applied and dried on one side of the biaxially oriented polyester film (b2) obtained above with a gravure roll coater so as to have a predetermined dry film thickness, and the resin layer (b1) after drying The film thickness was adjusted.
- the drying temperature was in the range of 80 to 120 ° C.
- the metal strip laminating apparatus shown in FIG. 1 is used to heat the chrome-plated steel sheet 1 obtained above with a metal band heating apparatus 2, and the container is formed on one surface of the chrome-plated steel sheet 1 with a laminating roll 3.
- the polyester film (A) that becomes the inner surface side was laminated (heat fusion), and the polyester film (B) that became the outer surface side of the container was laminated (heat fusion) on the other surface.
- the surface temperature of the metal plate is in the range of Tm to Tm + 40 ° C. of the polyester resin layer (a1) constituting the polyester film (A) except for some comparative examples. Controlled.
- the surface temperature of the laminate roll 3 was in the range of Tg to Tg + 60 ° C. of the polyester film (A), and the contact time with the metal plate was in the range of 10 to 15 msec.
- the Tg of the resins listed in Table 1 was almost no difference and was about 75 ° C.
- the laminating roll 3 is an internal water cooling type, and the cooling water is circulated in the roll to control the temperature during film bonding.
- the temperature of the resin layer before lamination was in the range of Tg + 30 ° C. to Tg + 100 ° C. of the polyester film (A), and the temperature distribution in the cross section of the resin layer was made uniform.
- water cooling was performed with the metal band cooling device 5, and the resin-coated metal plate for containers was manufactured.
- the production conditions are shown in Table 5.
- the cross-sectional structure of the resin-coated metal plate for containers manufactured as described above is shown in FIG.
- Raman band intensity 1615 cm -1 as I ND by measuring, determine the specific (I MD / I ND), to determine the maximum value and the average value of the intensity ratio (I MD / I ND).
- Raman band intensity at 1615 cm -1 (I MD and I ND) is high Satoshi the highest peak of the Raman band in the range of 1615 cm -1 ⁇ 10 cm -1, by the following equation, Raman band intensity ratio (I MD / IND ).
- I IMD / IND I MD : Raman band intensity of 1615 cm ⁇ 1 by polarization measurement parallel to the longitudinal direction
- I ND Raman band intensity of 1615 cm ⁇ 1 by polarization measurement parallel to the thickness direction (measurement conditions)
- salted meat for luncheon meat (protein content in solid content: 60 mass%) was filled into the cup, and the lid was wound up, followed by retort sterilization (130 ° C., 90 minutes). Then, when the lid was removed and the contents were taken out with the cup upside down, the degree of ease of taking out the contents was evaluated by observing the degree of the contents remaining inside the cup.
- ⁇ The contents remain inside the cup just by turning the cup upside down, but the contents can be taken out by vibrating the cup up and down (such as shaking the cup by hand).
- the retort sterilization treatment was performed at 130 ° C. for 90 minutes, and then aged for 90 days in a constant temperature bath at 38 ° C. Then, the can was opened and a sample for peel test (width 15 mm, length 120 mm) was cut from the can body. Part of the film is peeled off from the long side end of the cut sample. The peeled film was opened in the direction opposite to the peeled direction (angle: 180 °), and a peel test was performed using a tensile tester at a tensile speed of 30 mm / min. To evaluate the adhesion per 15 mm width. .
- the evaluation target surface is a can body portion on the inner surface of the can.
- Adhesion after molding 2 Cans that were moldable (greater than or equal to) in the moldability evaluation of (3) above were targeted.
- a sample for peel test (width 15 mm, length 120 mm) was cut out from the can body. Part of the film was peeled off from the long side end of the cut sample. The peeled film is opened in the direction opposite to the peeled direction (angle: 180 °), and using a tensile tester, a tensile speed of 30 mm / min.
- a peel test was conducted to evaluate the adhesion per 15 mm width.
- the evaluation object is the can body part on the outer surface of the can.
- Score Score
- A 10.0 (N) or more
- B 5.0 (N) or more, less than 10.0 (N) x: less than 5.0 (N) (7)
- Corrosion resistance 1 Cans that were moldable (greater than or equal to) in the moldability evaluation of (3) above were targeted.
- the lid was wrapped and sealed.
- the retort sterilization treatment was performed at 130 ° C. for 90 minutes, and then aged for 90 days in a constant temperature bath at 38 ° C.
- the evaluation target surface is a can body portion on the inner surface of the can.
- ⁇ Less than 1 mass ppm ⁇ : 1 mass ppm or more and less than 10 mass ppm ⁇ : 10 mass ppm or more
- Corrosion resistance 2 Cans that were moldable (greater than or equal to) in the moldability evaluation of (3) above were targeted. As shown in FIG. 3, crosscut scratches reaching the base steel plate were made at two locations on the can body on the outer surface of the can.
- the salt spray test based on JISZ2371 was performed with respect to the can which provided the crosscut damage
- the measurement method is shown in FIG.
- the evaluation object is the can body part on the outer surface of the can. (About the score) A: Maximum corrosion width on one side of less than 0.5 mm B: Maximum corrosion width on one side of 0.5 mm to less than 1.0 mm X: Maximum corrosion width on one side of 1.0 mm or more The results obtained above are shown in Tables 6 and 7.
- Metal plate manufacturing method A metal plate was produced in the same manner as in Example 1.
- a polyester compound obtained by polymerizing the acid component and glycol component shown in Table 8 at a ratio shown in Table 8 is blended with a wax compound to obtain a resin composition.
- This resin composition is dried and melted according to a conventional method, and extruded. After being cooled and solidified on a cooling drum to obtain an unstretched film, biaxial stretching and heat setting were performed to obtain a biaxially stretched polyester film (A).
- a polyester resin obtained by polymerizing the acid component and glycol component shown in Table 9 and further the wax compound in the ratio shown in Table 9 is dried and melted according to a conventional method, and coextruded from a T die, and then cooled on a cooling drum. After solidifying to obtain an unstretched film, biaxial stretching and heat setting were performed to obtain a biaxially stretched polyester film (b2).
- polyester resins, phenol resins, metal alkoxide compounds and / or metal chelate compounds, epoxy resins, polyamine resins, polyamidoamine resins, polyamide resins and colorants shown in Tables 10 and 11 are ratios shown in Tables 10 and 11.
- a synthesis example of a polyester resin (I-1) containing a repeating unit derived from diphenolic acid is shown.
- an acid component 50 parts by mass of terephthalic acid, 112 parts by mass of isophthalic acid, 4.9 parts by mass of diphenolic acid, and 50 parts by mass of 2-ethyl-2-butyl-1,3-butanediol as a polyhydric alcohol component, , 99 parts by mass of 4-butanediol, 48 parts by mass of 1,4-cyclohexanedimethanol and 0.07 parts by mass of titanium tetrabutoxide were charged into a 2 L flask, and the temperature was gradually raised to 220 ° C. over 4 hours. Esterification was carried out.
- the polymerization was carried out under reduced pressure up to 10 mmHg over 30 minutes, the temperature was raised to 250 ° C., and the latter polymerization was carried out at 1 mmHg or less for 50 minutes.
- the polymerization under reduced pressure was stopped, the mixture was cooled to 220 ° C. under a nitrogen stream, 1.9 parts by mass of trimellitic anhydride was added, and the mixture was stirred at 220 ° C. for 30 minutes to perform carboxy group modification (post-addition), and then resin
- the polyester resin (I-1) having a number average molecular weight of 22,000, an acid value of 5 (mgKOH / g) and a glass transition temperature of 30 ° C. was obtained.
- Byron GK-640 number average molecular weight: 18000, glass transition temperature: 79 ° C., manufactured by Toyobo Co., Ltd.
- TD2495 paracresol type phenol resin, 50% normal butanol solution, manufactured by DIC Corporation, which is a commercial product, was used.
- metal chelate compound (III) commercially available TC-200 (titanium octylene glycol chelate, manufactured by Matsumoto Fine Chemical Co., Ltd.) or the like is used.
- metal alkoxide compound (c) commercially available ZA-65 (zirconium butoxide, Matsumoto Fine Chemical Co., Ltd.) was used.
- epoxy resin (IV) commercially available epiclone N-660 (cresol novolac type epoxy resin, 50% methyl ethyl ketone solution, manufactured by DIC Corporation) and commercially available YL6121H (biphenyl type epoxy resin, manufactured by Mitsubishi Chemical Corporation) was used.
- polyamine resin (V) a commercially available product EPICRON EXB-353 (manufactured by DIC Corporation) was used.
- a commercially available SUNMIDE 328A (manufactured by Air Products Japan Co., Ltd.) was used as the polyamide amine resin.
- polyamide resin commercially available polyamide L-15-3, manufactured by Sanyo Kasei Co., Ltd. was used.
- the coating liquid is applied and dried on one side of the biaxially oriented polyester film (b2) obtained above with a gravure roll coater so as to have a predetermined dry film thickness, and the resin layer (b1) after drying The film thickness was adjusted.
- the drying temperature was in the range of 80 to 120 ° C.
- the metal strip laminating apparatus shown in FIG. 1 is used to heat the chrome-plated steel sheet 1 obtained above with a metal band heating apparatus 2, and the container is formed on one surface of the chrome-plated steel sheet 1 with a laminating roll 3.
- the polyester film (A) that becomes the inner surface side was laminated (heat fusion), and the polyester film (B) that became the outer surface side of the container was laminated (heat fusion) on the other surface.
- the surface temperature of the metal plate is in the range of Tm to Tm + 40 ° C. of the polyester resin layer (a1) constituting the polyester film (A) except for some comparative examples. Controlled.
- the surface temperature of the laminate roll 3 was in the range of Tg to Tg + 60 ° C. of the polyester film (A), and the contact time with the metal plate was in the range of 10 to 15 msec.
- the Tg of the resins listed in Table 1 was almost no difference and was about 75 ° C.
- the laminating roll 3 is an internal water cooling type, and the cooling water is circulated in the roll to control the temperature during film bonding.
- the temperature of the resin layer before lamination was in the range of Tg + 30 ° C. to Tg + 100 ° C. of the polyester film (A), and the temperature distribution in the cross section of the resin layer was made uniform.
- water cooling was performed with the metal band cooling device 5, and the resin-coated metal plate for containers was manufactured. Manufacturing conditions are shown in Table 12.
- the cross-sectional structure of the resin-coated metal plate for containers manufactured as described above is shown in FIG.
- the resin-coated metal sheet for containers according to the present invention is suitable for container applications and packaging applications that require excellent contents removal. And it can use as a raw material for containers which perform drawing processing etc., especially a raw material for food can containers.
- Metal plate (chrome plated steel plate) 2 Metal belt heating device 3 Laminate roll 4a Polyester resin layer (A) 4b Polyester resin layer (B) 5 Metal band cooling device
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Abstract
Description
そこで、これらの問題を解決するため、塗装金属板に替わり、熱可塑性樹脂フィルムを加熱した金属板に積層してなる樹脂被覆金属板が開発され、現在、飲料缶用素材を中心として工業的に広く用いられている。
[1]金属板と、該金属板を容器に成形した際に容器内面となる側に、ポリエステルを主成分とする複層構造の樹脂層(A)を有する容器用樹脂被覆金属板であって、
1)前記樹脂層(A)は、テレフタル酸を85mol%以上含み、
2)前記樹脂層(A)は、少なくとも2層から構成され、かつ内容物と接する最上層の樹脂層(a1)が、ワックス化合物を、前記最上層の樹脂層(a1)に対して、0.10~2.0mass%含有し、
3)前記最上層の樹脂層(a1)に対して、ラマン分光法による1615cm-1のラマンバンドについて、長手方向のピーク強度(IMD)と厚み方向のピーク強度(IND)の比(IMD/IND)の最大値が、1.0以上4.0以下であり、
4)前記最上層の樹脂層(a1)の厚みが0.5μm以上10μm以下であり、
5)前記最上層の樹脂層(a1)の厚みを除く前記樹脂層(A)の厚みが5μm以上20μm以下である容器用樹脂被覆金属板。
[2]前記ワックス化合物は、カルナウバワックスを含有する前記[1]に記載の容器用樹脂被覆金属板。
[3]前記金属板を容器に成形した際に容器外面となる側に、ポリエステルを主成分とする複層構造の樹脂層(B)を有し、前記金属板と接する樹脂層(b1)が、下記(I)~(V)の成分を含有する前記[1]または[2]に記載の容器用樹脂被覆金属板。
(I)ポリエステル樹脂
(II)フェノール樹脂
(III)金属アルコキシド系化合物及び/または金属キレート化合物
(IV)エポキシ樹脂
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれる一種以上
[4]前記樹脂層(B)が、前記樹脂層(b1)と、該樹脂層(b1)の上層に形成されるポリエステルフィルム(b2)からなる前記[3]に記載の容器用樹脂被覆金属板。
[5]前記樹脂層(b1)を形成する樹脂成分の比率が、下記を満足する前記[3]または[4]に記載の容器用樹脂被覆金属板。
(I)ポリエステル樹脂:50~89mass%
(II)フェノール樹脂:10~45mass%
(III)金属アルコキシド系化合物及び/または金属キレート化合物:0.01~10mass%
(IV)エポキシ樹脂:0.5~20mass%
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれる一種以上:0.1~10mass%
[6]前記樹脂層(b2)中の樹脂は、ポリエチレンテレフタレートまたは共重合成分の含有率が6mol%未満である共重合ポリエチレンテレフタレートからなるポリエステル(i)と、ポリブチレンテレフタレートまたは共重合成分の含有率が5mol%未満である共重合ポリブチレンテレフタレートからなるポリエステル(ii)を混合した組成物であり、かつ、前記ポリエステル(i)の比率が60mass%以下、前記ポリエステル(ii)の比率が40mass%以上である前記[4]または[5]に記載の容器用樹脂被覆金属板。
[7]前記樹脂層(B)が、ワックス化合物を、前記樹脂層(B)に対して、5.0mass%以下含有する前記[3]~[6]のいずれかに記載の容器用樹脂被覆金属板。
[8]前記樹脂層(B)のうち、最上層を除く樹脂層(b1)および最上層の樹脂層(b2)に、もしくは最上層の樹脂層(b2)にワックス化合物を含有し、前記最上層の樹脂層(b2)がワックス化合物を、前記最上層の樹脂層(b2)に対して、5.0mass%以下含有する前記[7]に記載の容器用樹脂被覆金属板。
[9]前記ワックス化合物は、カルナウバワックスを含有する前記[7]または[8]に記載の容器用樹脂被覆金属板。
[10]前記[1]~[9]のいずれかに記載の容器用樹脂被覆金属板の製造方法であって、最上層の樹脂層(a1)に対して、ラマン分光法による1615cm-1のラマンバンドについて、長手方向のピーク強度(IMD)と厚み方向のピーク強度(IND)の比(IMD/IND)の最大値が、1.0以上4.0以下の範囲となるように樹脂層形成条件を決定する容器用樹脂被覆金属板の製造方法。
まず、本発明で用いる金属板について説明する。
本発明の金属板としては、缶用材料として広く使用されているアルミニウム板や軟鋼板等を用いることができる。特に、下層が金属クロム、上層がクロム水酸化物からなる二層皮膜を形成させた表面処理鋼板(いわゆるTFS)等が最適である。
TFSの金属クロム層、クロム水酸化物層の付着量については、特に限定されないが、加工後密着性、耐食性の観点から、何れもCr換算で、金属クロム層は70~200mg/m2、クロム水酸化物層は10~30mg/m2の範囲とすることが望ましい。
本発明では、金属板を容器に成形した際に容器内面となる側に、ポリエステルを主成分とする複層構造の樹脂層(A)を有する。この樹脂層(A)は、ジカルボン酸成分とグリコール成分からなるポリマーであり、ジカルボン酸成分としてテレフタル酸85mol%以上含むことを特徴とする。テレフタル酸が、85mol%未満であった場合、樹脂の融点が低下し、容器成形時の摩擦熱で樹脂が軟化してしまい、フィルム削れ等の損傷が発生する懸念がある。また、容器成形後のレトルト殺菌処理においても、水蒸気により樹脂層がアタックされ、湿潤環境下での密着性が劣化する懸念がある。
また、本発明では、前記樹脂層(A)は、少なくとも2層から構成され、かつ内容物と接する最上層の樹脂層(a1)が、ワックス化合物を、前記最上層の樹脂層(a1)に対して、0.10~2.0mass%含有することを特徴とする。ワックス化合物を添加する目的は、樹脂層(A)の表面自由エネルギーを低下させることにあり、ワックス化合物を添加することにより樹脂層(A)に内容物が付着し難くなり、内容物取り出し性が向上する。0.10mass%以上に限定した理由は、0.10mass%未満となると、上記効果が乏しくなり、内容物の取り出し性が劣るためである。また、2.0mass%以下に限定した理由は、2.0mass%を超えると、フィルム成膜技術的にも困難な領域となるため、生産性に乏しくコスト高を招いてしまうためである。なお、最上層以外の樹脂層へのワックス添加の有無は特に限定するものではないが、添加する場合でも2.0mass%以下とすることが好ましい。ただし、最上層以外の樹脂層にワックス化合物を添加しても内容物取り出し性の向上効果は見られない場合があるため、最上層のみに添加することが効果的である。
さらに、前記最上層の樹脂層(a1)は、最上層の樹脂層(a1)に対して、ラマン分光法による1615cm-1のラマンバンド(I1615)について、長手方向(樹脂層(a1)表面と平行な方向)のピーク強度(IMD)と厚み方向(樹脂層(a1)表面と垂直な方向)のピーク強度(IND)の比(IMD/IND)の最大値が、1.0以上4.0以下であることを特徴とする。
樹脂層(a1)の厚みは、0.5μm以上10μm以下の範囲とする。ワックス化合物の添加量は、樹脂層(a1)に対して、2.0mass%以下に限定されるため、樹脂層(a1)の厚みが0.5μm未満となると、ワックスの含有量そのものが不足し、十分な内容物取り出し性が得られない。一方、10μm超となると、樹脂層(a1)の樹脂層(A)に対する比率が過度となり、樹脂層(A)と金属板との密着性や、樹脂層(A)の成形性、耐食性などの機能が低下する懸念がある。よって、樹脂層(a1)の厚みは、0.5μm以上10μm以下とする。
[最上層の樹脂層(a1)の厚み(平均膜厚)を除く樹脂層(A)の厚み(平均膜厚)]
最上層の樹脂層(a1)の厚みを除く樹脂層(A)の厚みは、5μm以上20μm以下とする。樹脂層(A)のうち、最上層の樹脂層(a1)を除く下層の樹脂層をa2とすると、厚みが5μm未満だと、樹脂層(a2)が金属板との密着性を確保しつつ樹脂層(a1)との界面密着性を保持するだけの樹脂強度が保てなくなる。一方、20μmを超えると、飲料缶用素材や食品缶詰用素材に求められる機能に対して、さらなる改善が望めないばかりか、樹脂コストの上昇のみを招いてしまう。よって、最上層の樹脂層(a1)の厚みを除く樹脂層(A)の厚み、すなわち、樹脂層(a2)の厚みは、5μm以上20μm以下とする。
金属板を容器に成形した際に容器外面となる側に、ポリエステルを主成分とする複層構造の樹脂層(B)を有し、前記金属板と接する樹脂層(b1)が、下記(I)~(V)の成分を含有することが好ましい。
(I)ポリエステル樹脂
(II)フェノール樹脂
(III)金属アルコキシド系化合物及び/または金属キレート化合物
(IV)エポキシ樹脂
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれる一種以上
樹脂層(B)はポリエステル樹脂を主成分とするが、ここで主成分とは樹脂被覆層(B)中の樹脂成分に50mass%以上のポリエステル樹脂を含むことを指す。
(I)ポリエステル樹脂
ポリエステル樹脂としては、数平均分子量3000~100000であることが好ましく、より好ましくは5000~30000、更に好ましくは10000~25000の範囲内である。なお、数平均分子量は、ゲル浸透クロマトグラフィー分析での、ポリスチレンとの比較による換算値である。数平均分子量が3000より低いと加工性が悪くなり、100000より高いと塗料化時の粘度が高くなり適切な塗装ができなくなる場合がある。
ポリエステル樹脂のガラス転移温度は、0℃以上100℃未満の範囲内であることが好ましい。ガラス転移温度が0℃以上100℃未満の範囲とすることで、樹脂の柔軟性・加工性や耐ブロッキング性が、適度にバランスされ、食品缶詰用途に好適となる。
1種のポリエステル樹脂では、数多い要求性能を満たすことが困難な場合がある。単独で使用した場合、例えば、ポリエステル樹脂のガラス転移温度が0℃以上35℃未満である場合、樹脂層に柔軟性が付与されるため加工性が優れる。しかし、フィルムに樹脂層をコーティングした後、巻かれた状態のままガラス転移温度を超える温度で長時間保持されると、フィルムがブロッキングしてしまうおそれがある。また、ガラス転移温度が低く、耐熱性が不足するため、耐レトルト性がやや劣るようになる。ガラス転移温度が35℃以上65℃未満である場合、フィルムがブロッキングせず、フィルムの美観が損なわれることがない。ガラス転移温度が65℃以上100℃未満である場合、ブロッキング性が優れるものの、皮膜が硬くなるためにやや加工性が劣るようになる。従って、ポリエステル樹脂はガラス転移温度が異なる複数の樹脂を併用して各々のポリエステル樹脂の良い性能を引き出すことで、バランスのとれた、より優れた樹脂層を得ることが好ましい。
ガラス転移温度が0℃以上35℃未満のポリエステル樹脂:30~80mass%
ガラス転移温度が35℃以上65℃未満のポリエステル樹脂:10~35mass%
ガラス転移温度が65℃以上100℃未満のポリエステル樹脂:10~35mass%
このような比率の範囲とすることで、加工性とブロッキング性のバランスが著しく向上する。
多価アルコール成分としては、エチレングリコール、ジエチレングリコール、プロピレングリコール、1、4ブタンジオール、ネオペンチルグリコール、3-メチルペンタンジオール、1、4-ヘキサンジオール、1、6-ヘキサンジオール、シクロヘキサンジメタノールなどの2価アルコールが主に用いられ、さらに必要に応じてグリセリン、トリメチロールエタン、トリメチロールプロパン、ペンタエリスリトールなどの3価以上の多価アルコールを併用することができる。これらの多価アルコールは単独で、または2種以上を混合して使用することができる。
樹脂層(b1)には、さらに成分(II)としてフェノール樹脂を添加することが好ましい。フェノール樹脂添加により架橋反応が起こり三次元的な網目構造を形成するため、皮膜の耐食性や耐レトルト性が向上する効果が得られる。石炭酸、m-クレゾール、m-エチルフェノール、3、5-キシレノール、m-メトキシフェノールなどの3官能のフェノール化合物、もしくは、p-クレゾール、o-クレゾール、p-tert-ブチルフェノール、p-エチルフェノール、2、3-キシレノール、2、5-キシレノール、m-メトキシフェノールなどの各種2官能性フェノールと、ホルムアルデヒドとをアルカリ触媒の存在下で合成したものが挙げられる。これらのフェノール化合物は、1種または2種以上を混合して使用することができる。また、フェノール樹脂に含有されるメチロール基の一部ないしまたは全部を、炭素数が1~12なるアルコール類によってエーテル化した形のものを使用することができる。
金属アルコキシド系化合物及び/または金属キレート化合物は、(I)ポリエステル樹脂、(II)フェノール樹脂、(IV)エポキシ樹脂と反応を起こす。各々の樹脂の官能基と金属アルコキシド系化合物及び/または金属キレート化合物の間で架橋反応が進行する。この架橋反応は、金属アルコキシド系化合物及び/または金属キレート化合物が無い場合と比較して、その皮膜の硬化速度が著しく速いために、結果として極めて少ない熱エネルギーで優れた密着性、加工性、耐レトルト性、耐食性を発現することが可能となる。例えば、既存のラミネート缶はフィルムをラミネートした後に180℃以上で、数秒~数分間焼付けが施され、その後の後加熱を利用し樹脂皮膜を硬化させ、上記の各種要求性能を確保するものである。しかし、本発明において、金属アルコキシド系化合物及び/または金属キレート化合物を含有した場合の樹脂層は、熱融着ラミネートを行う際の、1秒程度の短時間加熱のみで樹脂層が十分に硬化し、後加熱を施したものと同等以上の性能を得ることができる。したがって、製造プロセスにおける後加熱工程が不要となり、製造効率が格段に向上する。加えて、二酸化炭素の排出低減も可能となり、実用上極めて有用な技術となりうる。更に、皮膜中に金属が組み込まれることで、皮膜の強度が向上し、結果として耐衝撃性や耐食性が大幅に向上する。以上の理由により、前記樹脂層(b1)は、金属アルコキシド系化合物及び/または金属キレート化合物を含有することが好ましい。
金属アルコキシド系化合物及び/または金属キレート化合物としては、例えば、アルミニウム、チタン、錫、ジルコニウムなどのアルコキシド金属化合物、アセト酢酸が金属に配位した金属キレート化合物などが挙げられる。中でも、チタンアルコキシド系化合物及び/またはチタンキレート化合物を用いるのが好ましい。以下、その理由について説明する。
金属アルコキシド系化合物及び/または金属キレート化合物と、ポリエステル樹脂及び/またはフェノール樹脂とが連続的に架橋反応することで、分子鎖の三次元ネットワークが樹脂層内に形成される。これにより、レトルト処理環境下での水蒸気や熱水の浸透による変色を、最も効果的に抑制することが可能となる。水蒸気による変色とは、レトルト殺菌処理中に、樹脂層そのものが白く濁ったように変色する現象であり、レトルト白化と呼ばれている。これは缶外面の意匠性を損なわせるため、消費者の購買意欲を減退させうる大きな問題である。発明者らが鋭意検討した結果、缶体を被覆する樹脂層内に水蒸気が浸透することによって、樹脂層の界面及び界面近傍に液胞が形成され、液胞部で光が散乱することが原因であると考えられる。したがって、特性改善のためには、樹脂層の界面及び界面近傍での液胞形成を抑制することが重要である。すなわち、樹脂中に侵入した水蒸気は、樹脂中を拡散し、金属板との界面まで到達する。レトルト処理の開始直後は、缶内に充填された内容物が常温に近い状態にあるため、缶の外部から内部にかけて温度勾配が生ずる。即ち、樹脂中を拡散する水蒸気は、金属板に近づくにつれて冷却されることになり、金属板との界面及び界面近傍で液化し、凝縮水となって液胞を形成する。液胞がレトルト処理後も界面及び界面近傍に残留することで、光の散乱を招き、樹脂表面が白濁してみえることとなる。したがって、レトルト白化を抑制するためには、金属板との界面及び界面近傍における液胞の形成を抑止すればよい。
エポキシ樹脂は、主に皮膜の密着性を向上させるものである。特にノボラック型エポキシ樹脂であることが好ましい。ノボラック型エポキシ樹脂の市販品としては、DIC(株)製のエピクロンN-665、670、673、680、690、695、730、740、770、865、870、ダウケミカル(株)製のXD-7855、旭化成エポキシ(株)製のECN-1273、1299などが挙げられる。ビフェニル型エポキシ樹脂としては、三菱化学(株)製のYL6121H、YX7399が挙げられる。また、エポキシ樹脂はビスフェノールA以外であることが好ましい。ビスフェノールAは、内分泌撹乱作用が懸念されているためである。
ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂は、メラミン樹脂などと比較して硬化速度が速く、強靭な皮膜を形成できる点で優れている。ポリエステル/メラミン系、エポキシ/メラミン系等からなる樹脂組成物と比較して、硬化特性が優れるため、ラミネート鋼板の耐レトルト性、耐食性及び加工性の点で、特に優れた性能を発揮することが可能となる。
樹脂層(b1)を形成する樹脂成分の比率は、下記を満足することが好ましい。
(I)ポリエステル樹脂:50~89mass%
(II)フェノール樹脂:10~45mass%
(III)金属アルコキシド系化合物及び/または金属キレート化合物:0.01~10mass%
(IV)エポキシ樹脂:0.5~20mass%
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれるいずれか一種以上:0.1~10mass%
(I)ポリエステル樹脂の比率が50mass%より低いと加工性が悪化し、89mass%を超えると硬化性が不足し耐レトルト性が低下する場合がある。より好ましくは55~85mass%の範囲である。
(II)フェノール樹脂の比率が10mass%より低いと硬化性が不足し耐レトルト性が劣り、45mass%を超えると加工性が悪化する場合がある。より好ましくは20~40mass%である。
(III)金属アルコキシド系化合物及び/または金属系キレート化合物の比率が0.01mass%よりも低いと期待した速硬化性等の効果が得られない場合がある。10mass%を超えると樹脂皮膜が硬くなり加工性が劣るようになるのに加え、コーティング液作製時にゲル化を引き起こす場合がある。より好ましくは0.10~7mass%である。
(IV)エポキシ樹脂の比率が0.5mass%よりも低いと密着性が低下し結果として耐食性が劣化するようになり、20mass%を超えると耐レトルト白化性が低下してしまう場合がある。より好ましくは2~7mass%である。
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれる一種以上の比率が、0.1mass%より低いと硬化性が不足し耐レトルト性が劣り、10mass%を超えると加工性が悪化する場合がある。より好ましくは1~4mass%である。
樹脂層(b1)の厚み(平均膜厚)は、0.1μm以上5.0μm以下の範囲に規定するのが好ましい。0.1μm未満では、金属板表面を均一に被覆することができず、膜厚が不均一になる場合がある。一方、5.0μm超とすると、樹脂の凝集力が不十分となり、樹脂層の強度が低下してしまう恐れがある。その結果、製缶加工時に、樹脂層が凝集破壊してフィルムが剥離し、そこを起点に缶胴部が断裂してしまうことになる。
以上より、膜厚(平均膜厚)は、好ましくは0.1μm以上5.0μm以下、さらに好ましくは0.1μm以上3.0μm以下、より一層好ましくは0.5μm以上2.5μmである。なお、樹脂層(b1)の付着量としては、膜成分の比重により膜厚から換算できるが、本発明の成分配合の場合、ほぼ比重が1として換算しても問題ない。
樹脂層(b1)に染料、顔料などの着色剤を添加することで、下地の金属板を隠蔽し、樹脂独自の多様な色調を付与できる。例えば、黒色顔料として、カーボンブラックを添加することで、下地の金属色を隠蔽するとともに、黒色のもつ高級感を食品缶詰に付与することができる。
黒色顔料以外にも、白色顔料を添加することで下地の金属光沢を隠蔽するとともに、印刷面を鮮映化することができ、良好な外観を得ることができる。添加する顔料としては、容器成形後に優れた意匠性を発揮できることが必要であり、かかる観点からは、二酸化チタンなどの無機系顔料を使用できる。着色力が強く、展延性にも富むため、容器成形後も良好な意匠性を確保できるので好適である。
樹脂層(b1)には、前記の成分(I)~(V)及び着色剤に加えて、架橋を促進させる硬化触媒を添加することができる。例えば、リン酸等の無機酸、ドデシルベンゼンスルホン酸、トルエンスルホン酸等の有機酸及びこれらをアミン等でブロックしたものを使用することができる。硬化触媒の配合比率は、樹脂層(b1)中の樹脂量に対して、0.01~5PHRが好ましい。
ポリエステルフィルム(b2)の組成としては、ポリエチレンテレフタレートまたは共重合成分の含有率が6mol%未満である共重合ポリエチレンテレフタレート(以下、ポリエステル(i)と記載する場合もある)とポリブチレンテレフタレート(以下、ポリエステル(ii)と記載する場合もある)とを混合したポリエステル組成物であり、且つ、ポリエステル(i)の比率が60mass%以下、ポリエステル(ii)の比率が40mass%以上であることが好ましい。このような樹脂組成とすることで、食品缶詰用途で必須となるレトルト殺菌処理において、金属板との密着性を維持し、かつ、水蒸気が樹脂層内で凝結することによる樹脂変色を安定的に抑制することが可能となる。
[ワックス化合物]
さらに、本発明では、高加工時の樹脂層(B)の傷や削れを防ぐために、ワックス化合物を、樹脂層(B)に対して、5.0mass%以下含有することが好ましい。含有量が5.0mass%を超えると、容器外面に印刷や印字をする際に、樹脂層(B)とインクの密着性が劣化するため、印刷用途向けには好ましくない。また、樹脂層(B)の成膜性も困難になるため、好ましくない。一方、ワックス化合物の含有量が0.02mass%未満であると、ワックス化合物添加による樹脂層(B)の疵や削れ防止の効果が得られない場合があるため、ワックス化合物を含有する場合は0.02mass%以上とすることが好ましい。
次に本発明の容器用樹脂被覆金属板の製造方法について説明する。
まず、金属板に被覆する複層構造の樹脂層(A)(B)(フィルムの場合も含む)の製造方法について説明する。
樹脂層(A)(B)の製造方法については特に限定はしない。例えば、各ポリエステル樹脂等を必要に応じて乾燥した後、フィルム成分を公知の溶融積層押出機に供給し、スリット状のダイからシート状に押出し、静電印加等の方式によりキャスティングドラムに密着させ冷却固化し未延伸フィルム(シート)を得る。複層フィルムを得る場合は、積層押出機に、目的のフィルム成分を投入し、複層構成の未延伸フィルムを得る。この未延伸フィルムを長手方向及び幅方向に延伸することにより二軸延伸フィルムを得る。延伸倍率は目的とするフィルムの配向度、強度、弾性率等に応じて任意に設定することができる。フィルムの品質の点でテンター方式によるものが好ましい。長手方向に延伸した後、幅方向に延伸する逐次二軸延伸方式、長手方向、幅方向をほぼ同じに延伸していく同時二軸延伸方式が好ましい。
樹脂層の複層構造(2層以上)の形成方法についても特に限定するものではないが、一例として、樹脂層(b1)を、ポリエステルフィルム(b2)の表面に形成する方法について述べる。主成分となるポリエステル樹脂を有機溶媒中に溶解させるとともに、本発明が規定する樹脂層(b1)の添加成分及び任意添加成分を有機溶剤中に溶解または分散させてコーティング液を調製する。このコーティング液を、ポリエステルフィルム(b2)製膜時もしくは製膜後に、フィルム表面に塗布し乾燥することで、樹脂層(b1)を形成する。
本発明では、例えば、金属板をフィルムの融点を超える温度まで加熱し、圧着ロール(以後、ラミネートロールと称す)を用いて樹脂フィルムをその両面に接触させ熱融着させる方法(以後、ラミネートと称す)を用いことができる。このとき、容器成形した後に容器内面側になるフィルムについては、ワックス化合物が添加されていない樹脂層(a2)側を、金属板に接触させ熱融着させる。
(金属板の製造方法)
冷間圧延、焼鈍、調質圧延を施した厚さ0.18mm、幅977mmからなる鋼板を、脱脂、酸洗後、クロムめっきを行い、クロムめっき鋼板(TFS)を製造した。クロムめっきは、CrO3、F-、SO4 2-を含むクロムめっき浴でクロムめっき、中間リンス後、CrO3、F-を含む化成処理液で電解した。その際、電解条件(電流密度・電気量等)を調整して金属クロム付着量とクロム水酸化物付着量を、Cr換算でそれぞれ120mg/m2、15mg/m2に調整した。
表1に示す酸成分とグリコール成分を、酸成分でテレフタル酸以外の共重合成分はすべてエチレングリコールと重合させ、ポリエチレンテレフタレートまたは共重合ポリエチレンテレフタレートとし、さらに、テレフタル酸とブチレングリコールを重合したポリブチレンテレフタレートを混合し、ポリエステル樹脂とした。このポリエステル樹脂に、ワックス化合物を配合して樹脂組成物とし、この樹脂組成物を常法に従い、乾燥・溶融させ、押出した後、冷却ドラム上で冷却固化させ、未延伸フィルムを得た後、ニ軸延伸・熱固定して、ニ軸延伸ポリエステルフィルム(A)を得た。
表2に示す酸成分とグリコール成分を、酸成分でテレフタル酸以外の共重合成分はすべてエチレングリコールと重合させ、ポリエチレンテレフタレートまたは共重合ポリエチレンテレフタレートとし、さらに、テレフタル酸とブチレングリコールを重合したポリブチレンテレフタレートを混合し、ポリエステル樹脂とした。このポリエステル樹脂を常法に従い、乾燥・溶融させ、Tダイより共押出した後、冷却ドラム上で冷却固化させ、未延伸フィルムを得た後、ニ軸延伸・熱固定して、ニ軸延伸ポリエステルフィルム(b2)を得た。
ここで、ジフェノール酸に由来する繰り返し単位を含有したポリエステル樹脂(I-1)の合成例を示す。酸成分として、テレフタル酸50質量部、イソフタル酸112質量部、ジフェノール酸、4.9質量部、多価アルコール成分として2-エチル-2-ブチル-1、3-ブタンジオール50質量部、1、4-ブタンジオール99質量部、1、4-シクロヘキサンジメタノール48質量部、チタンテトラブトキシド0.07質量部を2Lフラスコに仕込み、4時間かけて220℃まで徐々に昇温し、水を留出させエステル化を行った。所定量の水を留出させた後、30分かけて10mmHgまで減圧重合を行うとともに温度を250℃まで昇温し、更にこのまま1mmHg以下で50分間後期重合を行った。ついで減圧重合を止めて、窒素気流下で220℃まで冷却し、無水トリメリット酸1.9質量部を添加し、220℃で30分攪拌しカルボキシ基変性(後付加)を行った後、樹脂を取り出し数平均分子量22000、酸価5(mgKOH/g)、ガラス転移温度30℃のポリエステル樹脂(I-1)を得た。この後、60℃以下まで冷却し、メチルエチルケトン/トルエン=50/50(質量%)の混合溶液で希釈し、不揮発分40%のポリエステル樹脂(I-1)溶液を得た。
図1に示す金属帯のラミネート装置を用い、前記で得たクロムめっき鋼板1を金属帯加熱装置2で加熱し、ラミネートロール3で前記クロムめっき鋼板1の一方の面に、容器成形した後に容器内面側になるポリエステルフィルム(A)をラミネート(熱融着)するとともに、他方の面に容器外面側になるポリエステルフィルム(B)をラミネート(熱融着)した。
ポリエステルフィルム(A)を金属板にラミネートする際に、金属板の表面温度は、一部の比較例を除き、ポリエステルフィルム(A)を構成するポリエステル樹脂層(a1)のTm~Tm+40℃の範囲に制御した。また、ラミネートロール3の表面温度は、ポリエステルフィルム(A)のTg~Tg+60℃の範囲とし、金属板との接触時間は、10~15msecの範囲とした。なお、表1に記載の樹脂のTgは、ほとんど差はなく、75℃程度であった。ラミネートロール3は、内部水冷式であり、ロール内に冷却水を循環させることで、フィルム接着中の温度制御を図った。ラミネート前の樹脂層の温度は、ポリエステルフィルム(A)のTg+30℃~Tg+100℃の範囲とし、樹脂層断面内の温度分布の均一化を図った。その後、金属帯冷却装置5にて水冷を行い、容器用樹脂被覆金属板を製造した。製造条件を、表5に示す。
以上より製造された容器用樹脂被覆金属板の断面構造を図2に示す。
以上より得られた樹脂被覆金属板及び金属板上に有する樹脂層に対して以下の特性を測定、評価した。測定、評価方法を、下記に示す。
ラミネート鋼板をエポキシ樹脂に包埋した後、湿式研磨し、断面は長手方向と平行にした。容器内面側樹脂層表面方向に対して平行なレーザー偏光面で、最上層の樹脂層(a1)の表面から厚み方向に対し、1μm毎の間隔で、1615cm-1のラマンバンド強度を測定してIMDとし、容器内面側樹脂層表面方向に対して垂直なレーザー偏光面で、最上層の樹脂層(a1)の表面から厚み方向に対し、1μm毎の間隔で、1615cm-1のラマンバンド強度を測定してINDとして、比(IMD/IND)を求め、この強度比(IMD/IND)の最大値と平均値を求めた。なお、1615cm-1でのラマンバンド強度(IMDおよびIND)は、1615cm-1±10cm-1の範囲 でのラマンバンドの最も高いピークの高さとし、下記式により、ラマンバンド強度比(IMD/IND)を求めた。
I=IMD/IND
IMD:長手方向に平行な偏光測定による1615cm-1のラマンバンド強度
IND:厚み方向に平行な偏光測定による1615cm-1のラマンバンド強度
(測定条件)
励起光源:半導体レーザー(λ=530nm)
顕微鏡倍率:×100
露光時間 :5秒
露光回数 :2回
アパーチャ:25μmφ
(2)内容物取り出し性
絞り成形機を用いて、ラミネート金属板を、絞り工程で、ブランク径:100mm、絞り比(成形前径/成形後径):1.88でカップ成形した。続いて、ランチョンミート用の塩漬け肉(固形分中のたんぱく質含有率:60mass%)をカップ内に充填し、蓋を巻き締めた後、レトルト殺菌処理(130℃、90分間)を行なった。その後、蓋を取り外し、カップを逆さまにして内容物を取り出した時に、カップ内側に残存する内容物の程度を観察することにより、内容物の取り出し易さの程度を評価した。
(評点について)
◎:カップをさかさまにしただけで(手で振ることなく)内容物が取り出せ、取り出し後のカップ内面を肉眼で観察した際、付着物が殆ど確認できない状態になるもの。
○:カップをさかさまにしただけではカップ内側に内容物が残存するが、カップを上下に振動させる(手でカップを振るなどの動作をする)と、内容物が取り出せる。取り出し後のカップ内面を肉眼で観察した際、付着物が殆ど確認できない状態になるもの。
×:カップを上下に振動させる(手でカップを振るなどの動作をする)だけでは、内容物が取り出し難い。上下に振動させるスピードを極端に増すか、もしくはスプーンなどの器具を用いて内容物を強制的に取り出した後、カップ内面を肉眼で観察した際、付着物が明らかに確認できる状態になるもの
(3)成形性
樹脂被覆金属板にワックス塗布後、直径165mmの円板を打ち抜き、絞り比1.50で浅絞り缶を得た。次いで、この絞り缶に対し、絞り比1.80及び2.00で再絞り加工を行った。この後、常法に従いドーミング成形を行った後、トリミングし、次いでネックイン-フランジ加工を施し深絞り缶を成形した。このようにして得た深絞り缶のネックイン部に着目し、フィルムの加工状態を目視観察した。
(評点について)
◎:成形後フィルムに損傷が認められない状態
○:成形可能であるが、部分的にフィルムの変色が認められる状態
×:缶が破胴し、成形不可能
(4)耐レトルト白化性
上記(3)の成形性評価で成形可能(○以上)であった缶の、底部(缶外面側)を対象とした。缶内に常温の水道水を満たした後、蓋を巻き締めて密閉した。その後、缶底部を下向きにして、蒸気式レトルト殺菌炉の中に配置し、125℃で90分間、レトルト処理を実施した。処理後、缶底部外面の外観変化を観察した。
(評点について)
◎:外観変化なし
○:外観にかすかな曇りあり
×:外観が白濁(白化発生)
(5)成形後密着性1
上記(3)の成形性評価で成形可能(○以上)であった缶を対象とした。缶の内部に、3質量%NaCl+3質量%クエン酸ナトリウム混合液を充填した後、蓋を巻き締めて密閉した。続いて、レトルト殺菌処理を130℃、90分間の条件で実施した後、38℃の恒温槽内で、90日間、経時させた。その後、缶を切り開き、缶胴部より、ピール試験用のサンプル(幅15mm、長さ120mm)を切り出した。切り出したサンプルの長辺側端部からフィルムの一部を剥離する。剥離したフィルムを、剥離された方向とは逆方向(角度:180°)に開き、引張試験機を用いて、引張速度30mm/min.でピール試験を行い、幅15mmあたりの密着力を評価した。評価対象面は、缶内面の缶胴部である。
(評点について)
◎:10.0(N)以上
○:5.0(N)以上、10.0(N)未満
×:5.0(N)未満
(6)成形後密着性2
上記(3)の成形性評価で成形可能(○以上)であった缶を対象とした。缶胴部よりピール試験用のサンプル(幅15mm、長さ120mm)を切り出した。切り出したサンプルの長辺側端部からフィルムの一部を剥離した。剥離したフィルムを、剥離された方向とは逆方向(角度:180°)に開き、引張試験機を用いて、引張速度30mm/min.でピール試験を行い、幅15mmあたりの密着力を評価した。評価対象は、缶外面の缶胴部である。
(評点)
◎:10.0(N)以上
○:5.0(N)以上、10.0(N)未満
×:5.0(N)未満
(7)耐食性1
上記(3)の成形性評価で成形可能(○以上)であった缶を対象とした。缶の内部に、市販のケチャップ(カゴメ(株)製)を充填した後、蓋を巻き締めて密閉した。続いて、レトルト殺菌処理を130℃、90分間の条件で実施した後、38℃の恒温槽内で、90日間、経時させた。その後、内容物(ケチャップ)中に溶出した鉄濃度を計測し、耐食性を評価した。評価対象面は、缶内面の缶胴部である。
(評点について)
◎:1質量ppm未満
○:1質量ppm以上10質量ppm未満
×:10質量ppm以上
(8)耐食性2
上記(3)の成形性評価で成形可能(○以上)であった缶を対象とした。図3に示すように、缶外面の缶胴部2箇所に、下地鋼板に達するクロスカット傷を入れた。続いて、クロスカット傷を付与した缶に対し、JISZ2371に準拠した塩水噴霧テストを300時間行い、傷部からの片側最大腐食幅を測定した。測定方法を図4に示す。評価対象は、缶外面の缶胴部である。
(評点について)
◎:片側最大腐食幅0.5mm未満
○:片側最大腐食幅0.5mm以上~1.0mm未満
×:片側最大腐食幅1.0mm以上
以上により得られた結果を表6、7に示す。
樹脂被覆金属板にワックス塗布後、直径179mmの円板を打ち抜き、絞り比1.80で浅絞り缶を得た。次いで、この絞り缶に対し、絞り比2.40及び3.00で再絞り加工を行い、深絞り缶を成形した。このようにして得た深絞り缶の缶胴部分に着目して、フィルムの加工状態を目視観察した。
(評点について)
◎:成形後フィルムに損傷が認められない状態
○:成形可能であるが、部分的にフィルムに僅かな傷が認められる状態
△:成形可能であるが、フィルムに削れが発生し、鋼板が部分的に露出している状態
×:缶が破胴し、成形不可能
(10)印刷適性
樹脂被覆金属板を容器成形した後に容器外面側となる樹脂表面に印刷用インク(東洋インキ(株)製印刷用インキCCST39) を塗布し、乾燥させ、塗膜厚1.5μmとなるよう調整した。
その後、塗装面にニチバン(株)製セロテープ(登録商標)を密着させ、一気に剥離した。
10枚試験を行い、インクが剥がれた枚数を調査した。
○ :0枚
△ :1~3枚
× :4枚以上
実施例1と同様の方法にて、金属板を製造した。
表8に示す酸成分とグリコール成分を、表8に示す比率にて重合したポリエステル樹脂に、ワックス化合物を配合して樹脂組成物とし、この樹脂組成物を常法に従い、乾燥・溶融させ、押出した後、冷却ドラム上で冷却固化させ、未延伸フィルムを得た後、ニ軸延伸・熱固定して、ニ軸延伸ポリエステルフィルム(A)を得た。
表9に示す酸成分とグリコール成分、さらにはワックス化合物を、表9に示す比率にて重合したポリエステル樹脂を常法に従い、乾燥・溶融させ、Tダイより共押出した後、冷却ドラム上で冷却固化させ、未延伸フィルムを得た後、ニ軸延伸・熱固定して、ニ軸延伸ポリエステルフィルム(b2)を得た。
ここで、ジフェノール酸に由来する繰り返し単位を含有したポリエステル樹脂(I-1)の合成例を示す。酸成分として、テレフタル酸50質量部、イソフタル酸112質量部、ジフェノール酸、4.9質量部、多価アルコール成分として2-エチル-2-ブチル-1、3-ブタンジオール50質量部、1、4-ブタンジオール99質量部、1、4-シクロヘキサンジメタノール48質量部、チタンテトラブトキシド0.07質量部を2Lフラスコに仕込み、4時間かけて220℃まで徐々に昇温し、水を留出させエステル化を行った。所定量の水を留出させた後、30分かけて10mmHgまで減圧重合を行うとともに温度を250℃まで昇温し、更にこのまま1mmHg以下で50分間後期重合を行った。ついで減圧重合を止めて、窒素気流下で220℃まで冷却し、無水トリメリット酸1.9質量部を添加し、220℃で30分攪拌しカルボキシ基変性(後付加)を行った後、樹脂を取り出し数平均分子量22000、酸価5(mgKOH/g)、ガラス転移温度30℃のポリエステル樹脂(I-1)を得た。この後、60℃以下まで冷却し、メチルエチルケトン/トルエン=50/50(質量%)の混合溶液で希釈し、不揮発分40%のポリエステル樹脂(I-1)溶液を得た。
図1に示す金属帯のラミネート装置を用い、前記で得たクロムめっき鋼板1を金属帯加熱装置2で加熱し、ラミネートロール3で前記クロムめっき鋼板1の一方の面に、容器成形した後に容器内面側になるポリエステルフィルム(A)をラミネート(熱融着)するとともに、他方の面に容器外面側になるポリエステルフィルム(B)をラミネート(熱融着)した。
ポリエステルフィルム(A)を金属板にラミネートする際に、金属板の表面温度は、一部の比較例を除き、ポリエステルフィルム(A)を構成するポリエステル樹脂層(a1)のTm~Tm+40℃の範囲に制御した。また、ラミネートロール3の表面温度は、ポリエステルフィルム(A)のTg~Tg+60℃の範囲とし、金属板との接触時間は、10~15msecの範囲とした。なお、表1に記載の樹脂のTgは、ほとんど差はなく、75℃程度であった。ラミネートロール3は、内部水冷式であり、ロール内に冷却水を循環させることで、フィルム接着中の温度制御を図った。ラミネート前の樹脂層の温度は、ポリエステルフィルム(A)のTg+30℃~Tg+100℃の範囲とし、樹脂層断面内の温度分布の均一化を図った。その後、金属帯冷却装置5にて水冷を行い、容器用樹脂被覆金属板を製造した。製造条件を、表12に示す。
以上より製造された容器用樹脂被覆金属板の断面構造を図2に示す。
以上より得られた樹脂被覆金属板及び金属板上に有する樹脂層に対して以下の特性を測定、評価した。測定、評価方法は、実施例1と同様である。
(2)内容物取り出し性
(3)成形性
(4)耐レトルト白化性
(5)成形後密着性1
(6)成形後密着性2
(7)耐食性1
(8)耐食性2
(9)成形加工時の耐傷付き性
(10)印刷適性
2 金属帯加熱装置
3 ラミネートロール
4a ポリエステル樹脂層(A)
4b ポリエステル樹脂層(B)
5 金属帯冷却装置
Claims (10)
- 金属板と、該金属板を容器に成形した際に容器内面となる側に、ポリエステルを主成分とする複層構造の樹脂層(A)を有する容器用樹脂被覆金属板であって、
1)前記樹脂層(A)は、テレフタル酸を85mol%以上含み、
2)前記樹脂層(A)は、少なくとも2層から構成され、かつ内容物と接する最上層の樹脂層(a1)が、ワックス化合物を、前記最上層の樹脂層(a1)に対して、0.10~2.0mass%含有し、
3)前記最上層の樹脂層(a1)に対して、ラマン分光法による1615cm-1のラマンバンドについて、長手方向のピーク強度(IMD)と厚み方向のピーク強度(IND)の比(IMD/IND)の最大値が、1.0以上4.0以下であり、
4)前記最上層の樹脂層(a1)の厚みが0.5μm以上10μm以下であり、
5)前記最上層の樹脂層(a1)の厚みを除く前記樹脂層(A)の厚みが5μm以上20μm以下である
容器用樹脂被覆金属板。 - 前記ワックス化合物は、カルナウバワックスを含有する請求項1に記載の容器用樹脂被覆金属板。
- 前記金属板を容器に成形した際に容器外面となる側に、ポリエステルを主成分とする複層構造の樹脂層(B)を有し、前記金属板と接する樹脂層(b1)が、下記(I)~(V)の成分を含有する請求項1または2に記載の容器用樹脂被覆金属板。
(I)ポリエステル樹脂
(II)フェノール樹脂
(III)金属アルコキシド系化合物及び/または金属キレート化合物
(IV)エポキシ樹脂
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれる一種以上 - 前記樹脂層(B)が、前記樹脂層(b1)と、該樹脂層(b1)の上層に形成されるポリエステルフィルム(b2)からなる請求項3に記載の容器用樹脂被覆金属板。
- 前記樹脂層(b1)を形成する樹脂成分の比率が、下記を満足する請求項3または4に記載の容器用樹脂被覆金属板。
(I)ポリエステル樹脂:50~89mass%
(II)フェノール樹脂:10~45mass%
(III)金属アルコキシド系化合物及び/または金属キレート化合物:0.01~10mass%
(IV)エポキシ樹脂:0.5~20mass%
(V)ポリアミン樹脂、ポリアミドアミン樹脂、ポリアミド樹脂からなる群から選ばれる一種以上:0.1~10mass% - 前記樹脂層(b2)中の樹脂は、ポリエチレンテレフタレートまたは共重合成分の含有率が6mol%未満である共重合ポリエチレンテレフタレートからなるポリエステル(i)と、ポリブチレンテレフタレートまたは共重合成分の含有率が5mol%未満である共重合ポリブチレンテレフタレートからなるポリエステル(ii)を混合した組成物であり、かつ、前記ポリエステル(i)の比率が60mass%以下、前記ポリエステル(ii)の比率が40mass%以上である請求項4または5に記載の容器用樹脂被覆金属板。
- 前記樹脂層(B)が、ワックス化合物を、前記樹脂層(B)に対して、5.0mass%以下含有する請求項3~6のいずれか一項に記載の容器用樹脂被覆金属板。
- 前記樹脂層(B)のうち、最上層を除く樹脂層(b1)および最上層の樹脂層(b2)に、もしくは最上層の樹脂層(b2)にワックス化合物を含有し、
前記最上層の樹脂層(b2)がワックス化合物を、前記最上層の樹脂層(b2)に対して、5.0mass%以下含有する請求項7に記載の容器用樹脂被覆金属板。 - 前記ワックス化合物は、カルナウバワックスを含有する請求項7または8に記載の容器用樹脂被覆金属板。
- 請求項1~9のいずれか一項に記載の容器用樹脂被覆金属板の製造方法であって、最上層の樹脂層(a1)に対して、ラマン分光法による1615cm-1のラマンバンドについて、長手方向のピーク強度(IMD)と厚み方向のピーク強度(IND)の比(IMD/IND)の最大値が、1.0以上4.0以下の範囲となるように樹脂層形成条件を決定する容器用樹脂被覆金属板の製造方法。
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WO2024209846A1 (ja) * | 2023-04-06 | 2024-10-10 | Jfeスチール株式会社 | 樹脂被覆金属板及びその製造方法 |
Also Published As
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CA2937215A1 (en) | 2015-08-27 |
CA2937215C (en) | 2019-01-29 |
AU2015220290B2 (en) | 2017-07-13 |
JP5812232B1 (ja) | 2015-11-11 |
EP3109042B1 (en) | 2019-10-16 |
CN106029368A (zh) | 2016-10-12 |
CN106029368B (zh) | 2018-09-14 |
US9873539B2 (en) | 2018-01-23 |
EP3109042A1 (en) | 2016-12-28 |
WO2015125185A1 (ja) | 2015-08-27 |
AU2015220290A1 (en) | 2016-07-21 |
EP3109042A4 (en) | 2017-03-22 |
PH12016501530B1 (en) | 2016-10-03 |
KR20160124196A (ko) | 2016-10-26 |
TWI558548B (zh) | 2016-11-21 |
TW201538312A (zh) | 2015-10-16 |
TW201532804A (zh) | 2015-09-01 |
JPWO2015125461A1 (ja) | 2017-03-30 |
KR101948149B1 (ko) | 2019-02-14 |
US20160355294A1 (en) | 2016-12-08 |
PH12016501530A1 (en) | 2016-10-03 |
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