GB2238507A - Copolyester resin film laminated metal sheet - Google Patents
Copolyester resin film laminated metal sheet Download PDFInfo
- Publication number
- GB2238507A GB2238507A GB8925353A GB8925353A GB2238507A GB 2238507 A GB2238507 A GB 2238507A GB 8925353 A GB8925353 A GB 8925353A GB 8925353 A GB8925353 A GB 8925353A GB 2238507 A GB2238507 A GB 2238507A
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- Prior art keywords
- resin film
- copolyester resin
- metal sheet
- copolyester
- sheet
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Classifications
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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
- B32B15/00—Layered products comprising a layer of metal
- B32B15/04—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B15/08—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
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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
- B32B15/00—Layered products comprising a layer of metal
- B32B15/04—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B15/08—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
- B32B15/09—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin comprising polyesters
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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
- B32B15/00—Layered products comprising a layer of metal
- B32B15/18—Layered products comprising a layer of metal comprising iron or 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
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
- B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/12—Bonding of a preformed macromolecular material to the same or other solid material such as metal, glass, leather, e.g. using adhesives
- C08J5/124—Bonding of a preformed macromolecular material to the same or other solid material such as metal, glass, leather, e.g. using adhesives using adhesives based on a macromolecular component
- C08J5/128—Adhesives without diluent
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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
- B32B2307/00—Properties of the layers or laminate
- B32B2307/50—Properties of the layers or laminate having particular mechanical properties
- B32B2307/514—Oriented
- B32B2307/518—Oriented bi-axially
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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
- B32B2367/00—Polyesters, e.g. PET, i.e. polyethylene terephthalate
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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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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
Abstract
Produced by a method comprising laminating a biaxially oriented copolyester resin film having specified characteristics, to one or both sides of a surface treated metal sheet, which has been heated to the melting point of the copolyester resin film +/- 50 DEG C, just before lamination of the copolyester resin film, the film having been precoated with a resin composite containing in its molecular structure at least one radical, such as epoxy radical and hydroxyl radical and the side of the copolyester resin film precoated with resin composite is in contact with the surface treated metal sheet.
Description
COPOLYESTER RESIN FILM LAMINATED METAL SHEET
The present invention relates to a copolyester resin film laminated metal sheet having excellent formability and its method of production. The process comprises laminating a biaxially oriented copolyester resin film, having specified characteristics, precoated with a small amount of a resin comp6site, the resin composite containing at least one radical, such as an epoxy radical or a hydroxyl radical on one or both sides of a surface treated metal sheet which has been heated to the melting point of the copolyester resin film + 500C just before the lamination of the copolyester resin film. The side of the copolyester resin film precoated with the resin composite is in contact with the surface treated metal sheet.
At present, metal sheets, such as electrotinplate, tin free steel and aluminum sheets are widely used for can stock after being coated, at least once, with lacquer. This lacquer coating is disadvantageous from an energy standpoint as significant time is required for curing the lacquer and large volumes of solvent discharged during the lacquer curing process must be burned in another furnace in order to prevent air pollution.
Recently, lamination of thermoplastic rein film on a metal sheet was attempted in order to avoid these problems. See for example, Laid-Open Japanese Patent Application No. Sho 53141786, Japanese Patent Publication No. Sho 60-47103, Laid-Open
Japanese Patent Application Nos. Sho 60-168643, Sho 61-20736 and
Sho 61-149341.
Laid-Open Japanese Patent Application No. Sho 53-141786 discloses a metal can produced from a metal sheet covered with polyolefin resin film, using an adhesive containing polyolefin resin modified with a carboxyl radical. However, this polyolefin film laminated metal sheet cannot be used as a material for can stock as the metal sheet can become corroded by the packed contents due to the poor permeability resistance of the laminated polyolefin resin film. Furthermore, even if the polyolefin resin film laminated metal sheet is used as a material for can stock, cans having satisfactory appearance cannot be obtained because the laminated polyolefin resin film is melted during heating at temperatures of from 160 to 200 0C . These temperatures are required for curing the printing ink or the coated lacquer.
Japanese Patent Publication No. Sho 60-47103 relates to a process for lamination of a crystalline polyester resin film to a metal sheet by heating the sheet above the melting point of said polyester resin film and thereafter immediately quenching the laminate. In this patent, the crystalline polyester film is sufficiently adhered to the metal sheet by an amorphous and nonoriented polyester resin film that is formed at the interface of the crystalline polyester film and the metal sheet as a result of the heating step. However, when the polyester film laminated metal sheet is reheated to 160 to 2000C for 10 to 30 minutes, as required for curing the printing ink or lacquer applied on the other side of the metal sheet before forming, adhesion of the polyester resin film deteriorates. This is due to the amorphous non-oriented polyester resin layer recrystallizing upon heating.As a result, corrosion resistance also deteriorates.
Laid-Open Japanese Patent Application No. Sho 60-168643 relates to a thermoplastic resin film laminated steel sheet for a drawn and ironed can (DI can) and the production method therefor.
In said patent, the side of the steel sheet to be employed for the inside of the DI can is laminated with a thermoplastic resin film, such as polyethylene terephthalate, without any adhesives. The side of the steel sheet to be employed for the outside of the DI can is plated with a ductile metal, such as tin, nickel or aluminum.
The steel sheet according to said patent has the same defects as those in Japanese Patent Publication No. Sho 60-47103, i.e., as a result of the reheating to the 160 to 2000C for 10 to 30 minutes required for curing the printing ink and the lacquer on the outside of the DI can, the adhesion of the polyester resin film noticeably deteriorates.
Laid-Open Japanese Patent Application Nos. Sho 61-20736 and Sho 61-149341 relate to lamination of a precoated biaxially oriented polyester resin films to a metal sheet heated below the melting point of said polyester resin film. The film is precoated with a special adhesive, such as an epoxy resin containing a curing agent. In said patent applications, an amorphous and non-oriented polyester resin layer as shown in Japanese Patent Publication
No. Sho 60-47103 and Laid-Open Japanese Patent Application No. So 60-168643 is not formed. This is because the lamination of biaxially oriented polyester resin film to the metal sheet is carried out below the melting point of said polyester resin film.Therefore, the corrosion resistance and the adhesion of polyester resin film to the metal sheet does not deteriorate, even if it is reheated at temperatures of 160 to 2O00C for the time required for curing printing ink and lacquer. However, if said laminated metal sheet is used for some applications requiring more severe formability, such as a deep drawn can having a drawing ratio higher than 2.0, many cracks occur in the polyester resin film.
Recently, the use of a polyester resin film haying specified characteristics has been proposed in order to improve the formability of the polyester resin film laminated metal sheet (Laid-Open Japanese Patent Application No. Sho 64-22530 and
Japanese Patent Application No. Sho 63-75837). However, when these polyester resin film laminated metal sheets are formed in processes such as deep drawing or bending at high speed, many cracks arise or the laminated polyester resin film is peeled off in the formed area of said polyester resin film.
Accordingly, it is the first objective of the present invention to provide a surface treated metal sheet covered with copolyester resin film having excellent corrosion resistance in a part formed under severe conditions, such as a deeply drawn can, a drawn and partially ironed can and a drawn and stretch formed can having a high can height and a drawing ratio above 2.0, even after reheating to cure overcoated color printing ink or lacquer.
It is the second objective of the present invention to provide a method for continuous high speed lamination of copolyester resin film on one or both sides of a surface treated metal sheet.
The first objective of the present invention can be accomplished by the formation of a film consisting of an outer layer and an inner layer on the surface of a metal layer. The outer layer is comprised of a copolyester resin film possessing specific characteristics and is produced by stretching and heat setting a copolyester resin film consisting of 75 to 99 mole % of polyethylene terephthalate and 25 to 1 mole % of a polyester resin produced by esterification of at least one saturated polycarboxylic acid with at least one saturated polyalcohol. The inner layer comprises a thin resin composite containing in its molecular structure, at least one radical, such as epoxy radical and hydroxyl radical. The composite layer is present on one or both sides of the surface treated metal sheet.
The second objective of the present invention can be accomplished by continuous high speed lamination of a copo3yester resin film precoated with resin composite, onto one or both sides of a surface treated metal sheet that has been heated to + 500C of the melting point of the copolyester resin film, with the precoated side of the copolyester resin film being in contact with the metal sheet.
The specific characteristics referred to sura are:
(1) melting temperature;
(2) refractive index of the film's thickness;
(3) refractive index of the film's planar dimensions;
and
(4) amount and average particle size of added lubricant,
when lubricant is added thereto.
The copolyester resin film laminated metal sheet having an excellent formability according to the present invention can be obtained by controlling all of these factors in the optimum ranges as disclosed below.
Thus, according to one aspect of the present invention we provide a copolyester resin film laminated metal sheet, comprising
(i) a biaxially oriented copolyester resin film having a melting point from about 210"C to about 250"C, a refractive index of from about 1.5000 to 1.5500 relative to the thickness of said film and a refractive index of from 1.6000 to 1.6600 relative to the planar dimensions of said films,
(ii) a resin composite which has been applied to at least one side of said copolyester resin film, said resin composite containing at least one radical selected from epoxy, hydroxyl, amide, ester, carboxyl, urethane, acryl and amino radicals, and
(iii) a surface treated metal sheet, at least one side of which is laminated to said side of said copolyester resin film which has said resin composite applied thereto.
The copolyester resin film laminated metal sheet according to the present invention can be used in applications .where excellent corrosion resistance is required after severe forming. Examples are deeply drawn cans, drawn and partially ironed cans, drawn and stretch formed cans having high can height and a high drawing ratio and can ends where a tab for easy opening is attached. In these applications, the cans are exposed to hot water or hot steam for sterilization after packing food, such as fruit juices, coffee drinks, meats and fish. For example, fruit juices are immediately packed in the can after sterilization, at a temperature of 90 to 100"C. Coffee drinks, meats and fish are sterilized by hot steam at a temperature above 100"C in a retort after being packed in the can.Furthermore, the metal sheet according to the present invention can be used for screw caps and crown caps.
In these applications, color printing ink or lacquer coating on one or both sides of the metal sheet used for the outside or inside of these cans is often carried out before or after forming. In these cases, the laminated copolyester resin film in the present invention is not peeled off in the severely formed areas, even after reheating for curing color printing ink or lacquer and subsequent treatment by hot water or hot steam.
The invention will now be described with reference to the accompanying drawing in which:
Figure 1 depicts, graphically, the relationship between the refractive index of a given copolymer and the degree of elongation possible before the copolymer film breaks.
The present invention is a laminated metal sheet where the metal sheet is laminated with copolyester resin film having specified characteristics. The copolyester resin film may consist of 75 to 99 mole % of polyethylene terephthalate and 25 to 1 mole % of a polyester resin produced by the esterification of at least one saturated polycarboxylic acid with at least one saturated polyalcohol selected from the following polycarboxylic acldsand polyalcohols.
Saturated polycarboxylic acids are preferably selected from phthalic acid, isophthalic acid, terephthalic acid, succinic acid, azel.aic acid, adipic acid, sebacic acid, diphenyl carboxylic acid, 2,6naphthalene dicarboxylic acid, 1,4-cyclohexane dicarboxylic acid and trimellitic acid anhydride.
Saturated polyalcohols are preferably selected from ethylene glycol, 1,4-butane diol, 1,5-pentane diol, 1,6-hexane diol, propylene glycol, polytetramethylene glycol, trimethylene glycol, triethylene glycol, neopenthyl glycol, 1,4-cyclohexane dimethanol, trimethylol propane and pentaerythritol.
Furthermore, in the present invention, the use of biaxially oriented copolyester resin film having all of the following factors in some optimum range is indispensable from the viewpoint of corrosion resistance after severe forming. These factors are:
(1) melting temperature;
(2) refractive index of the film's thickness;
(3) refractive index of the film's planar dimensions;
and
(4) amount and average particle size of added lubricant,
when lubricant is added thereto.
In some cases, additives such as antioxidants, stabilizer, pigments, antistatic agents and corrosion inhibitors may be added during the manufacturing process of the copolyester resin film.
The melting temperature of the employed copolyester resin film is defined as the temperature at which the endothermic peak is obtained at a heating rate of 10 OC/minute in the differential scanning calorimeter (SS10) made by Seiko Denski Kogyo.Co. It is preferred that a copolyester resin film having a melting temperature of from about 210 to about 2500C should be used. The use of a copolyester resin film having a melting temperature above 2500C is not suitable in the present invention as such rigid copolyester resin films have poor formability. A copolyester resin film having a melting temperature below 210 C is not practical as its mechanical property deteriorates upon the reheating required to cure the color printing ink or lacquer applied to the outside or inside of the can.
The refractive indices, the second and third factors mentioned, -may be measured by using a polarized monochromatic light in Abbeys refractometer at 250C.
In the biaxially oriented copolyester resin film used in the present invention, the refractive indices in the thickness direction and all planar dimensions in the plane should be in-the range of from about 1.5000 to about 1.5500 and from about 1.6000 to about 1.6600, respectively. These refractive indices change slightly depending upon conditions used to laminate the copolyester resin film to the metal sheet, as well as reheating conditions necessary to cure the color printing ink or lacquer applied to the copolyester resin film laminated metal sheet. The degree of change in the refractive index of said copolyester resin film also depends on the stretching conditions and heat setting conditions for the production of thin and wide copolyester resin film. For example, if the laminating temperature of the copolyester resin film is higher, the refractive index of the laminated copolyester resin film decreases. The refractive index of the copolyester resin film produced under lower stretching and heat setting at higher temperature decreases. On the other hand, the refractive index produced under higher stretching and heat setting at lower temperature increases.
As described above, the refractive index of the copolyester resin film is dependent upon the manufacturing conditions of copolyester resin film, the laminating conditions and the reheating conditions.
In the present invention, it is necessary that the refractive indices in the thickness direction and all planar dimensions of the copolyester resin film should be controlled in the range of from about 1.5000 to about 1.5500 and from about 1.6000 to about 1.6600, respectively, after lamination to the surface treated metal sheet. It is preferred that the refractive index in all directions in the plane of the copolyester resin film be maintained in the range of 1.6100 to 1.6500 after lamination, in order to obtain a copolyester resin film laminated metal sheet having excellent formability.
Copolyester resin films having refractive indices beyond the optimum range described above, are not practical for some applications where severe formability is required. Many cracks may arise in said copolyester resin film or the laminated copolyester resin film may be peeled off in the severe formed area as a result of the deterioration in formability.
Laid-Open Japanese Patent Application No. Sho 64-22530 and Japanese Patent Application No. Sho 63-75837 disclose polyester resin film laminated metal sheet having excellent formability.
The former patent application shows that a polyester resin film with excellent formability is obtained by controlling the planar orientation coefficient in the range of from 0.130 to 0.160. This planar orientation coefficient, which is defined as the degree of the planar coefficient of the polyester resin film, is determined by using a refractometer and is shown by the following equation:
A = (B+C)/2-D, where, A represents the planar orientation coefficient of the polyester resin film,
B represents the refractive index in the lengthwise direction of the polyester resin film,
C represents the refractive index in the widthwise direction of the polyester resin film, and
D represents the refractive index in the thickness direction of the polyester resin film.
Usually, the thin and wide polyester resin film is produced continuously by stretching the extruded thick polyester resin film in the lengthwise and widthwise directions. Therefore, the characteristics in the center position of the wide polyester resin film are different from those in the edge position, particularly, the mechanical property and the coefficient of expansion by heat in the oblique direction in the edge position of the wide film.
Even if the planar orientation coefficient in the center position of the wide polyester resin film is the same as that in the edge position, the characteristics in the center position are different from that in the edge position, because the planar orientation coefficient calculated by the equation described above is defined without consideration of the refractive index in the oblique direction of the polyester resin film. The latter patent application shows that a polyester resin film having excellent formability is obtained by controlling the melting temperature, the softening temperature and the elongation at break within the range of 210 to 2500C, 175 to 2350C and 150 to 400%, respectively.
Recently, it has been found that the elongation at break is related to the refractive index in the plane of the copolyester resin film as shown in Figure 1. In particular, the elongation at break declines if the refractive index in the plane falls below 1.6100. Even the copolyester resin film to be laminated on the metal sheet has above 150% of the elongation at break and excellent formability with a refractive index below 1.6100 in the plane. The corrosion resistance of the metal sheet covered with this copolyester resin film becomes poor in the areas formed under severe conditions, because the amorphous and non-oriented parts in this copolyester resin film increase if the refractive index decreases.Furthermore, the gradual decrease in the elongation at break when the refractive index is above 1.6200 depends upon the increase in the degree of orientation in the copolyester resin film.
Even if a copolyester resin film having above 150% of the elongation at break with a refractive index of 1.6700 in the plane is laminated on the metal sheet, a copolyester resin film laminated metal sheet having excellent formability is not always obtained.
This is because the elongation at break of said copolyester resin film decreases after lamination.
Therefore, a copolyester resin film laminated metal sheet having excellent formability is not always obtained by using the copolyester resin film according to Japanese Patent Application No.
Sho 63-75837, as the characteristics of the copolyester resin film change depending upon the laminating and reheating conditions.
This problem has been.solved by the present invention by controlling the characteristics of the employed copolyester resin film before and after lamination. According to the present invention, in a copolyester resin film laminated metal sheet, where formability under severe conditions is required, it is indispensable that the mechanical property, thermal property and chemical property of the employed copolyester resin film are uniform throughout.
Therefore, the copolyester resin film used in the present invention is characterized by the restriction in the range of the refractive indices in the thickness direction and all directions in the plane as has been described above.
In order to produce a copolyester resin film having excellent formability in all positions of the wide copolyester resin film, it is necessary that the extruded thick copolyester resin film is biaxially stretched with a lower ratio compared to that in usual polyethylene terephthalate film. For instance, it is desireable to stretch the extruded copolyester resin film 2.7 to 3.7 times in the lengthwise\ direction and about 3.0 to 3.8 times in the widthwise direction and that the temperature be set at from about 150 to about 2300C.
Additionally, the amount and the particle size of a lubricant in the copolyester resin are important factors when a lubricant is used. At least one lubricant selected from silica(SiO2), alumina, titanium dioxide, calcium carbonate, barium sulfate and organic silicon compound is usually added during the manufacturing process of the copolyester resin film, and it is desirable to use a lubricant having an average particle size below 2.5 pm, preferably 0.5 to 2.0 pm. It is not practical to use a lubricant having a particle size above 2.5 pm, as it acts as the starting point for the growth of many cracks in the laminated copolyester resin film during severe forming. Generally, the amount of lubricant added into the copolyester resin film is determined by the quality in coiling the produced copolyester resin film and formability of the copolyester resin film laminated metal sheet. If the lubricant is not added into the copolyester resin film, it is not possible to wind the produced copolyester resin film smoothly. Usually, the addition of lubricant having a large particle size is effective in small amounts. On the other hand, a lubricant having a small particle size, must be added in a larger quantity.For example, silica having an average particle size of 2.3 pm is effective with the addition of 0.001 to 0.05 weight % to the weight of the copolyesterxresin. In the case of silica having an average particle size of 0.3 pm, addition of 0.05 to 5 weight % to the weight of the copolyester resin is necessary.
Copolyester resin films to be used for the outside of cans, containing inorganic color pigment such as titanium dioxide (TiO2 powder), instead of coating a white enamel on the clear copolyester resin film laminated metal sheet and then curing the coated white enamel. It is desirable that the amount of the color pigment added to the copolyester resin film be 2 to 20 weight % relative to the weight of the copolyester resin. If the amount of color pigment is below 2 weight %, a satisfactory appearance is not obtained. The copolyester resin film containing color pigment above 20 weight % is not suitable in the present invention, as the formability of said film becomes noticeably poor.
Measurement of refractive indices of the copolyester resin film containing color pigment is not possible as the polarized monochromatic light used for measurement does not pass through the pigmented film. Therefore, it is necessary to produce the copolyester resin film containing color pigment under the same conditions as those for the clear copolyester resin film having the refractive indices described above.
The thickness of the copolyester resin film used in the present invention should preferably be 5 to 50 pm, more preferably 10 to 30 pm. If the thickness of the employed copo3yester resin film is below 5 pm, the excellent corrosion resistance after severe forming of the copolyester resin film laminated metal sheet is not obtained and continuous lamination of thin copolyester resin film to the surface treated metal sheet becomes noticeably difficult.
Moreover, the use of the copolyester resin film having a thickness above 50 pm is not economically suitable for lamination on surface treated metal sheet, as the copolyester resin film used for the present invention is expensive compared with epoxy phenolic lacquers widely used in the can industry.
One side of the copolyester resin film selected by the various characteristics described above, may be precoated with 0.1 to 5.0 g/m2 of a resin composite containing at least one radical or group selected or derived from an epoxy radical, a hydroxyl radical, an amide radical, an ester radical, a carboxyl radical, a urethane radical, an acryl radical and an amino radical. Epoxy resin, phenol resin, nylon resin, polyester resin, modified vinyl resin, urethane resin, acryl resin and urea resin are examples of such resin composites.
It is desirable that the resin composite be coated on one side of the copolyester resin film as uniformly and thinly as possible. This is because the bonding strength of resin composite layer to the surface treated metal sheet and the copolyester resin film becomes gradually poorer with an increase in the thickness of the precoated resin composite. However, it is very difficult to uniformly coat in amounts below 0.1 g/m2 of the resin composite on the copolyester resin film. Furthermore, when the amount of the resin composite is below 0.1 g/m2 or above 5.0 g/m2, the bonding strength of the resin composite layer to the surface treated metal sheet and the copolyester resin film becomes noticeably poor in severely formed areas.It is preferable that the resin composite be diluted by a solvent and then coated by a roller or spray method in order to form a uniform and thin resin composite layer on the copolyester resin film. The temperature for drying a resin composite diluted by a solvent which is coated on one side of the copolyester resin film is one of the important factors in the present invention. If the temperature is below 600C, a long time is required for the removal of solvent and the formed resin composite layer becomes tacky. When the drying temperature is above 150 0C, the chemical reaction of resin composite coated on the copolyester resin film is accelerated, and the bonding strength of the resin composite to the surface treated metal sheet becomes noticeably poor.It is preferable that the drying time of the resin composite solution coated on the copolyester resin film be 5 to 30 seconds at a temperature of 60 to 1500C. If the drying time is less than 5 seconds, the solvent is not sufficiently removed. On the other hand, drying times of more than 30 seconds result in poor productivity.
A solvent having low boiling point is preferred for dissolving the resin composite as it is easily removed by heating at 60 to 1500C. The solvent has no other specific limitations. In some cases, a coloring agent, such as a dye, may be added to the resin composite dissolved into the solvent.
The surface treated metal sheet should be selected from a tin free steel having double layers of an upper layer of hydrated chromium oxide and a lower layer of metallic chromium, electrotinplate covered with the double layer as described above, electrotinplate covered with hydrated chromium oxide and an aluminum sheet treated in a solution containing chromate, phosphate or zirconium salt which is usually used for the treatment of aluminum drawn and ironed cans, as the metal sheet of the present invention is contemplated for use in sanitary food containers such as cans.
The optimum range of hydrated chromium oxide and metallic chromium in a tin free steel is 5 to 25 mg/m2 hydrated chromium
oxidefand 10 to 150 mg/mZ as metallic chromium, respectively. If the amount of hydrated chromium oxide is below 5 mg/m or above 25 mg/m as chromium, the bonding strength to the copolyester resin film precoated with said resin composite becomes noticeably poor in severely formed areas. Although the corrosion resistance in the formed part becomes graauallypoorer with a decrease in the amount of metallic chromium, even tin free steel having about 10 mg/m2 of metallic chromium can be used for some applications where mild corrosion resistance is required.The electrotinplate should be cathodically treated in an electrolyte for producing an ordinary tin free steel or treated by immersion in a solution containing about 30 g/l of sodium dichromate in water. By said cathodic treatment, a double layer consisting of an upper layer of hydrated chromium oxide and a lower layer of metallic chromium is formed on the electrotinplate. It is desirable that the amount of hydrated chromium oxide and metallic chromium on electrotinplate be almost the same as that in tin free steel. However, it is preferable that the amount of metallic chromium be 10 to 50 mg/m2, in order to facilitate high speed production.
In the case of immersion treatment of electrotinplate in sodium dichromate solution, a thin layer of hydrated chromium oxide in an almost constant amount (1 to 4 mg/m2 as chromium) is formed on the electrotinplate. The thin hydrated chromium oxide on electrotinplate is necessary for excellent adhesion of the copolyester resin film precoated with said resin composite in severely formed area. If electrotinplate is not treated by immersion into sodium dichromate solution, the adhesion of the copolyester resin film precoated with said-resin composite becomes gradually poorer during storage in an atmosphere having high humidity.If hydrated chromium oxide, having above 5 mg/m2 as chromium, is formed on electrotinplate by cathodic treatment in sodium dichromate solution, adhesion of the copolyester resin film precoated with resin composite becomes noticeably poor in severely formed areas. It is considered that the difference in the adhesion of the copolyester resin film to electrotinplate depends on the quality of the hydrated chromium oxide. The hydrated chromium oxide formed by cathodic treatment in an electrolyte, for producing a tin free steel, has better adhesion to said copolyester resin film precoated with resin composite compared with that by an immersion treatment into sodium dichromate solution.
It is desirable in the present invention that the amount of plated tin in electrotinplate be from 0.5 to 5.6 g/m2. If the amount of plated tin is less than 0.5 g/m2, the effect of plated tin on the corrosion resistance is hardly apparent, despite further plating process. An amount of above 5.6 g/m2 of tin is not economical.
The temperature of the surface treated metal sheet heated just before the lamination of the copolyester resin film precoated with resin composite, is also an important factor. This should be maintained at the melting point of said copolyester resin filmy + 500C. If the temperature is50 C above the melting point corrosion resistance becomes noticeably poor as the copolyester resin film deteriorates by post-heating after lamination.
The copolyester resin film used in the present invention cannot be easily recrystallized by the heating temperature required for curing the color printing ink or lacquer applied on the metal sheet, although a non-oriented amorphous copolyester resin layer is formed by heating. Therefore, the metal sheet maintains excellent corrosion resistance, even if it is heated at 160 to 2000C. If the lamination of the copolyester resin film precoated with resin composite to the surface treated metal sheet is carried out 50"C bel.ow themelting temperature of the copolyester resin film the copolyester resin film is easily peeled off from the surface of the surface treated metal sheet.
In the present invent ion, the method for heating the surface treated metal sheet to which the copolyester resin film is laminated is not limited to any particular method. However, from the standpoint of continuous and stable production of the metal sheet at high speed, conduction heating by a roller heated by induction heating and induction heating and/or resistance heating which are used for reflowing electrotinplate in the production process of electrotinplate, is suitable as the method for heating the surface treated metal sheet to be laminated. This is because the surface treated metal sheet can be rapidly heated and the temperature of the heated metal sheet can be easily controlled. Furthermore, it is also preferable that heating by rollers heated by hot steam or heating for preheating the surface treated metal sheet to be laminated.
The surface temperature of the laminating roller is also an important factor . The surface temperature of the laminating roller should be in the range of 80 to 180 C. Below 800C, air bubbles may easily occur between the copolyester resin film precoated with resin composite and the surface treated metal sheet, when the copolyester resin film is laminated to the metal sheet.
On the other hand, at temperatures above 180 C, production of the metal sheet at high speed is prevented, because the copolyester resin film easily adheres to the laminating roller. The use of a chromium plated, ceramic or rubber laminating roller is preferable.
A roller made with silicon rubber or fluorine rubber, which are excellent in heat conductivity and heat resistance, should be selected.
Usually, the copolyester resin film is laminated on the surface treated metal under the conditions described above, and then the copolyester resin film laminated metal sheet is gradually or rapidly cooled. In some applications, where more severe formability is required, it is preferable to post-heat the copoRyester resin film laminated metal sheet at a temperature in the range of from the melting point -80 C to the melting point of the copolyester resin film for 5 to 1000 seconds, in order to improve the formability of the copolyester resin film laminated metal sheet. Heating in order to cure the color printing ink or lacquer applied on the copolyester resin film laminated metal sheet before forming is also effective in improving the formability of the copolyester resin film laminated metal sheet.Heating in order to cure the color printing ink or lacquer applied on the copolyester resin film laminated metal sheet before forming, is also effective in improving the formability of the copolyester resin film laminated metal sheet.
It is considered that this effect depends on the relaxation of the residual stress of the laminated copolyester by the post-heating. When this post-heating is applied to the copolyester resin film laminated metal sheet before forming, the laminated copolyester resin film is not peeled off from the surface of the metal sheet and cracks in the laminated copolyester resin film are almost non-existent in severely formed areas.
The present invention will now be explained in further detail by reference to the following non-limiting examples.
EXAMPLE 1
A cold rolled steelsstrip having a thickness of 0.21 mm and a width of 300 mm was electrolytically degreased in a solution of 70 g/l of sodium hydroxide and then pickled in a solution of 100 g/l of sulfuric acid. The steel strip, after being rinsed with water, was cathodically treated by using an electrolyte containing 60 g/l of Cr03 and 3 g/l of NaF in water under 20 A/dm2 of cathodic current density at an electrolyte temperature of 50 C. The treated steel strip was rinsed with hot water having a temperature of 80 C and dried.
After that, a biaxially oriented copolyester resin film produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 85 mole % of terephthalic acid and 15 mole % of sebacic acid having characteristics shown in (A), which was precoated with a resin composite under following condition (B), was continuously laminated on both surfaces of the treated steel strip under the following condition (C).
(A) Characteristics of the employed copolvester resin film
Thickness : 25 iim Melting temperature : 229 C Refractive index in thickness direction : 1.5311
Refractive index in all planar dimer.sions : Maximum : 1.6411
: Minimum : 1.6210
Type of added lubricant :Silica (SiO2)
Average particle sige of added lubricant : 2.0 m
Amount of lubricant: 0.07 weight % relative to
the weight of the employed copolyester (B) Conditions for precoating of resin composite to the copolyester resin film
Composition of precoated material:
Epoxy resin having an epoxy equivalent of 3000 : 80 parts
Resol product from paracresol : 20 parts
Drying temperature of precoated resin composite : 100 C Drying time of precoated resin composite : 10 seconds
Amount of resin composite after drying : 0.2 g/m2 (C) Conditions for lamination of copolvester resin film
precoated under condition (B)
Method for heating the treated steel strip
Roller heated by induction heating
Temperature of the treated steel strip just before
lamination : 200 C Material of laminating roller : Silicon rubber
Surface temperature of laminating roller : Max. 180 C Method for cooling after lamination : Rapid cooling
Post heating of the laminate : 215 C for 1 minute
EXAMPLE 2
Two kinds of biaxially oriented copolyester resin films produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 88 mole % of terephthalic acid and 12 mole % of isophthalic acid having characteristics shown in (A), which were precoated with resin composite by the following condition (B), were simultaneously laminated on each side of the same treated steel strip as in Example 1 under the following condition (C).
(A) Characteristics of the emPloyed copolyester resin
film
Clear film
Thickness : 25 pm Melting temperature : 229 C Refractive index in thickness direction : 1.5405
Refractive indices in all planar dimensions
: Maximum 1.6500
: Minimum 1.6305
Type of added lubricant : Silica (Si02) Average particle size of added lubricant
: 1.5 pm Amount of added lubricant : 0.12 weight % relative
to the weight of the employed copolyester resin
White film
Thickness : 20 pm Melting temperature : 229 C Type of color pigment :Tio2
Average particle size of added color pigment : 0.-3 pm Amount of added color pigment : 15 weight % relative to
the weight of the employed copolyester resin (B) Conditions for precoatinq of resin composite to the
copolvester resin films
Composition of precoated material
Epoxy having an epoxy equivalent of 3000 : 70 parts
Resol product from paracresol : 30 parts
Drying temperature of precoated resin composite
: 120 C Drying time of precoated resin composite : 5 seconds
Amount of resin composite after drying : 1.1 g/m2 (C) Conditions for lamination of conolvester resin film recoated under condition (B)
Method for heating the treated steel strip
Roller heated by induction heating
Temperature of the treated steel strip just before
lamination : 230 C Temperature of the treated steel strip just before
lamination : 230 C Material of laminating roller : Silicon rubber
Surface temperature of laminating roller
: Max. 210 C Method for cooling after lamination :Rapid cooling
Post heating of the laminate : 210 C for 5 minutes
EXAMPLE 3
The same steel strip pretreated as in Example 1 was electroplated with 2.8 g/m2 of tin by using an electrolyte containing 80 g/l of SnS04, 60 g/l of phenolsulfonic acid (60%) aqueous solution) and 5 g/l of a-naphthol sulfonic acid in water under 15 A/dm2 of cathodic current density at an electrolyte temperature of 40 C. After reflowing of tin and rinsing with water, the tin plated steel strip was treated by using an electrolyte containing 30 g/l of Cr03 and 0.3 g/l of H2SO in water under 40 A/dm2 of cathodic current density at an electrolyte temperature of 50 C. The thus treated electrotinplate was rinsed with water and dried.
After that, a biaxially oriented copolyester resin film produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 88 mole % terephthalic acid and 12 mole % of sebacic acid having characteristics shown in (A), which was precoated with resin composite by the following condition (B), was continuously laminated on both surfaces of thus treated steel strip under the following condition(C).
(A) Characteristics of the employed coolvester resin
film
Thickness : 25 pm Melting temperature : 243 'C
Refractive index in thickness direction : 1.5218
Refractive indices in all planar dimensions Maximum 1.6312
: Minimum 1.6228
Type of added lubricant :Silica (sio2) Average particle size of added lubricant
: 0.3 pm Amount of added lubricant: 0.81 weight % relative
to the weight of the employed copolyester
resin
(B) Conditions for precoatinq of resin composite to the conolvester resin film
Composition of precoated resin composite
Epoxy resin having an epoxy equivalent of 2500
: 75 parts
Resol product from paracresol : 25 parts
Drying temperature of precoated resin composite
: 75 C Drying time of resin composite after drying
:15 sec.
Amount of resin composite after drying: 1.2 g/m2
(C) Conditions for lamination of coDolvester resin film Drecoated under condition (B)
Method for heating the treated steel strip
: Resistance Heating
Temperature of the treated steel strip just before
lamination : 228 C Material of laminating roller : Silicon rubber
Surface temperature of laminating roller : 200 C Method for cooling after lamination: Gradual
cooling
Post heatirig of the laminate: 2200C for 30 seconds
EXAMPLE 4
The same steel strip pretreated as in Example 1 was electroplated with 1.5 g/m2 of tin by using an electrolyte containing 10 g/l of SnS04, 20 g/l of phenolsulfonic acid (60% aqueous solution) and 4 g/l of ethoxylated a-naphthol in water under 3 A/dm2 of cathodic current density at an electrolyte temperature of 45 C. After rinsing with water, the tin plated steel strip was treated by an immersion into 30 g/l of sodium dichromate solution for 3 seconds at a temperature of 45 C. The thus treated electrotinplate strip was rinsed with water and dried.
After that, a biaxially oriented copolyester resin film produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 80 mole % of terephthalic acid and 20 mole % of sebacic acid having characteristics shown in (A), which was precoated with the same resin composite as in Example 3, was continuously laminated on both surfaces of thus treated steel strip under the following condition (C).
(A) Characteristics of the employed coPolvester resin film
Thickness: 25 pm Melting temperature: 2150C
Refractive index in thickness direction :1.5100
Refractive indices in all planar dimensions
: Maximum 1.6211
: Minimum 1.6110
Type of added lubricant : TiO2 Average particle size of added lubricant: 0.5 pm Amount of added lubricant: 0.52 weight % relative to the
weight of the employed copolyester resin
(B) Conditions for lamination of cotolvester resin film.
precoated under condition (B) of Example 3
Method for heating the treated steel strip
: Resistance heating
Temperature of the treated steel strip just before
lamination : 234 0C Material of laminating roller: Fluorine rubber
Surface temperature of laminating roller: 1800C
Method for cooling after lamination: Rapid cooling
Post heating of the laminate: 1900C for 30 seconds
EXAMPLE 5
An aluminum strip (JIS 3004) having a thickness of 0.23 mm was cathodically degreased in a solution of 30 g/l of sodium carbonate. After being rinsed with water, the aluminum strip was immersed into 5% Alodine 401-41 (Chromate-Phosphate type) solution made by Nippon Paint Co., Ltd. for 20 seconds at 450C and then rinsed with water and dried.
After that, the same biaxially oriented copolyester resin film as shown in (A) of Example 1, which was precoated with the same resin composite as in (B) of Example 1, was continuously laminated on both surfaces of thus treated aluminum strip under the same conditions as in condition (C) of Example 1.
COMPARATIVE EXAMPLE 1
A biaxially oriented copolyester resin film produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 85 mole % of terephthalic acid and 15 mole % of sebacic acid having characteristics shown in (A), which was precoated with the same resin composite as in Example 1, was continuously laminated on both surfaces of the same treated steel strip as in Example 1 under the same conditions as in (C) of Example 1.
(A) Characteristics of the employed copolyester resin film
Thickness: 25 pm Melting temperature: 2290C
Refractive index in thickness direction: 1.5334
Refractive indices in all planar dimensions
: Maximum 1.6473
: Minimum 1.6022
Type of added lubricant:Silica (SiO2)
Average particle size of added lubricant: 2.0 pm Amount of added lubricant: 0.07 weight % relative to the
weight of the employed copolyester resin
COMPARATIVE EXAMPLE 2
A biaxially oriented copolyester resin film produced from a condensation polymerizaiton of the ethylene glycol and polycarboxylic acid consisting of 88 mole % terephthalic acid and 12 mole % of isophthalic acid having characteristics shown in (A), which was precoated with the same resin composite as in Example 1, was continuously laminated on both surfaces of the same treated steel strip as in Example 1 under the same conditions as in condition (C) of Example 1.
(A) Characteristics of the employed copolvester resin film
Thickness : 25 pm Melting temperature; 2290C
Refractive index in thickness direction : 1.5110
Refractive indices in all planar dimensions
: Maximum 1.6720
: Minimum 1.6390
Type of added lubricant:Silica
Average particle size of added lubricant: 2.0 iim Amount of added lubricant: 0.07 weight % relative to the
weight of the employed copolyester resin
COMPARATIVE EXAMPLE 3
A biaxially oriented copolyester resin film produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 83 mole % of terephthalic acid and 17 mole % of isophthalic acid having characteristics shown in (A), which was precoated with the same resin composite as in Example 3, was continuously laminated on both surfaces of the same treated steel strip as in Example 3 under the same conditions as in condition (C) of Example 3.
(A) Characteristics of the employed copolyester resin film
Thickness: 25 m
Melting temperature: 212 C
Refractive index in thickness direction : 1
Refractive indices in all directions in the plane
: Maximum 1.6041
: Minimum 1.5986
Type of added lubricant: Silica
Average particle size of added lubricant: 2.3 Um Amount of added lubricant: 0.07 weight % relative to the
weight of the employed copolyester resin
COMPARATIVE EXAMPLE 4
A biaxially oriented copolyester resin film produced from a condensation polymerization of ethylene glycol and polycarboxylic acid consisting of 85 mole % of terephthalic acid and 15 mole % of sebacic acid having characteristics shown in (A), which was precoated with the same resin composite as in Example 3, was continuously laminated on both surfaces of the same treated steel strip as in Example 4 under the same conditions as condition (B) of Example 4.
(A) Characteristics of the employed copolyester resin film
Thickness : 25 m
Melting temperature: 2150C
Refractive index in thickness direction: 1.53il Refractive indices in all directions in the plane
: Maximum 1.6331
: Minimum 1.6098
Type of added lubricant: Silica
Average particle size of added lubricant: 2.9 pm Amount of added lubricant: 0.05 weight % relative to
the weight of the employed copolyester resin
COMPARATIVE EXAMPLE 5
The same biaxially oriented copolyester resin film as in
Example 1, which was precoated with the same resin composite as in
Example 1, was continuously laminated on both surfaces of the same treated aluminum strip as in Example 5 under the same conditions as in Example 1, except that the termperature of the treated aluminium strip just before laminationwas 1620C.
The formability and the corrosion resistance of the resultant metal sheet were evaluated by the following testing methods, after the measurement of the coating weight on the resultant metal sheet by X=ray fluorescent method. The results are shown in the Table.
(1) Formability by deep drawing
The resultant metal sheet was cut by a punch press, to a circular blank having a diameter of 158 mm. The blank was deeply drawn to form a cylindrical cup at a drawing ratio of 2.92. The formability of the resultant metal sheet was evaluated by the degree of cracks in the copolyester resin film and the degree in the peeling off of the copolyester resin film in the formed area and then divided into 5 ranks. 5 was excellent, 4 was good, 3 was fair, 2 was poor and 1 was bad.
(2) Formability by impact bending
The resultant metal sheet was cut to a size of 30 mm x 50 mm.
The sample was pre-bent by a rod having a diameter of 3 mm and was then bent by dropping a load weighing 2.3 kg from a height of 30 cm. The formability, by bending the resultant metal sheet, was evaluated by the degree of cracks in the copolyester resin film in the bent area by use of a microscope. It was then divided into the 5 ranks, as described above.
(3) Corrosion resistance after cup drawing
The resultant metal sheet was cut by a punch press to a circular blank having a diameter of 85 mm. The blank was deeply drawn to form a cylindrical cup at a drawing ratio of 2.15. The drawn cup was filled with Coca Cola and stored at 200C. After 3 months, iron pick-up was measured by using an atomic absorption method.
The terms and expressions which have been employed are used as terms of description and not of limitation, and there is no intention in the use of such terms and expressions of excluding any equivalents of the features shown and described or portions thereof, it being recognized that various modifications are possible within the scope of the invention.
TABLE 1
Comp. Comp. u) Ex.1 Ex.2 g ow c( LO re I oJ ( Q, a o C)Or U) d Base metal Steel Steel Steel Steel Al Steel Steel Steel Steel Al V Sn X o o H 000a0 0 v Coating 0 0 2.8 1.5 n 2.8 1.5 weight Cr Cr v, Cr+PO Cr crP ~ O W V1 L O O cu (gim' ) re 0.120 H H H X C ~ U) O O O O Cr Cr O Cr D O Oi0 0.015 < D O O X 0% 0.003 0.015 0.015 O.'010 0.003 e cn u, m o O 1i1 0 C N 0 O o O . . . O U) Q RI in thickness f.
~ direction O e O O H 1.5520 1.5180 1.5390 1.5330 1.5311 - N O N ~ X 0% ~s Zq -u O d D a X Max. RI q plane 1.6395 1.6510 1.6358 1.6115 1.6390 1.6?11 1.6790 1.5960 1.6300 1.6389 o on No o u uo rtre ~ o Min. E in plane 1.6180 1.6311 1.6300 1.6005 1.6175 1.5g00 1.6411 1.5900 1.6081 1.6195 -O ure urcO (D a- o re O V1 O 0) O re e X w w -b ~ e e e o O by deep drawing 5 5 5 5 5 . . 2 5 1 O UU r(lr( tr 6 Formability by . impact bending 5 5 5 5 5 re 1 5 o W ce 6 U H Corr. resistance Fe < C) pick up) 0.02 0.01 0 0 0 30.6 106.3 50.6 2.80 Delami.
sr o o ZD ~s O . @ . e o H H o uz uo o X 4) B e s t n s: H v o . . . @ zn U t < H H N ~ o o e o ) @ H H ax u: O . @ so o o ~ n ) uo uo o 8 w ' e ' 5 ' sD 0 eJ) < N o O o O . . . @ 0 U Q H ~l ~l eh ~ O U) e O H b1 < 1} N H 'O > H H ~r . @ ~{ O X U) n U) U) O K < v u O .
0 o0 o0 . . . s0 O o ~h ~ ~ e H O U) O UW O ~s O < O 0 > X N . O ~s O X X ~s U) U) O u) o o o o . . . @ o ~ C) U H H H X @ bO eb < g: 1: eo u ~ DD < ~ > < g o ~ . F3 C ~ ~ 3 D ~ d S ~ x > s o : e.x w 00 U < t g: : r r @ ~ tJ < J 00 ~ O ~ ~ z n e ~ < J: J: ~ ffi ~ @ G z ee w w H ~ ~ @ ç w o o o ~ tD A: X D @ D O ~z e ç C @ ht f Z @ < : a o 3 ~ o . . E fi ss o f0 t.) ~ AC 1 o > o E o tD ~a z o n o - cx X K z z X X t~ > laays IelaW R tTJ UTSa - savlaadold JaXsatodo Remarks: *1 RI represents the refractive index.
*2 Cr@ represents metallic Cr and Crox represents Cr in hydrated Cr oxide.
*3 Fe and Al pick up is shown by ppm.
Claims (21)
1. A copolyester resin film laminated metal sheet, comprising
(i) a biaxially oriented copolyester resin film having a melting point from about 210"C to about 250"C, a refractive index of from about 1.5000 to 1.5500 relative to the thickness of said film and a refractive index of from 1.6000 to 1.6600 relative to the planar dimensions of said film,
(ii) a resin composite which has been applied to at least one side of said copolyester resin film, said resin composite containing at least one radical selected from epoxy, hydroxyl, amide, ester, carboxyl, urethane, acryl and amino radicals, and
(iii) a surface treated metal sheet, at least one side of which is laminated to said side of said copolyester resin film which has said resin composite applied thereto.
2. A sheet as claimed in claim 1, wherein said copolyester resin film further comprises a lubricant having a particle size below about 2.5 ssm.
3. A sheet as claimed in claim 1 or claim 2, having a refractive index in its planar dimension of from 1.6100 to 1.6500.
4. A sheet as claimed in any of the preceding claims, wherein said copolyester resin film comprises from about 75 to about 99 mole percent of polyethylene terephthalate and from about 1 to 25 mole percent of a polyester resin produced by esterification of at least one saturated polycarboxylic acid selected from phthalic acid, isophthalic acid, terephthalic acid, succinic acid, azelaic acid, adipic acid, sebacic acrid, diphenylcarboxylic acid, 2,6-naphthalene dicarboxylic acid, 1,4-cyclohexane dicarboxylic acid and trimellitic acid anhydride with at least one saturated polyalcohol selected from ethylene glycol, 1,4-butane diol, 1,5pentane diol, 1,6-hexane diol, propylene glycol, polytetramethylene glycol, trimethylene glycol, triethylene glycol, neopentyl glycol, 1,4-cyclohexane dimethanol, trimethylol propane and pentaerythritol.
5. A sheet as claimed in any of the preceding claims wherein said copolyester resin film has a thickness of from about 5 to about 50 pm.
6. A sheet as claimed in any of the preceding claims wherein said resin composite is present in an amount ranging from about 0.1 to about 5.0 g/m2 of said copolyester resin film.
7. A sheet as claimed in any of the preceding claims wherein said surface treated metal sheet is selected from a tin free steel having double layers of an upper layer of hydrated chromium oxide and a lower layer of metallic chromium, an electrotinplate covered with said double layers, an electrotinplate covered with hydrated chromium oxide and an aluminum treated in a solution containing chromate, phosphate or zirconium salt, of said metal sheet.
8. A sheet as claimed in claim 7 wherein said hydrated chromium oxide is present in an amount ranging from about 5 to about 25 mg/m2 as chromium of said treated metal sheet and said metallic chromium is present in an amount from about 10 to about 150 mg/m2 of said treated metal sheet in said double layers.
9. A sheet as claimed in claim 7 wherein said treated metal sheet is an electrotinplate and said electrotinplate is coated with a tin coating in an amount ranging from about 0.5 to about 5.6 g/m2 of said treated metal sheet.
10. A sheet as claimed in claim 8 or claim 9 wherein said hydrated chromium oxide on said electrotinplate is present in an amount of from about 1 to about 4 mg/m2 as chromium.
11. A sheet as claimed in any of the preceding claims wherein said copolyester resin film contains from about 2 to about 20 weight percent of an inorganic pigment.
12. A sheet as claimed in claim 11 wherein said inorganic pigment is titanium dioxide.
13. A copolyester resin film laminated metal sheet substantially as herein described with reference to the
Examples.
14. A method for the production of a copolyester resin film as claimed in claim 1, comprising
i) precoating at least one side of a copolyester resin film as defined in claim 1 with a resin composite as defined in claim 1;
ii) heating a surface treated metal sheet to a temperature within the melting point of said copolyester resin film +50 c, and
iii) contacting the side of said copolyester resin film treated with said resin composite to at least one side of said surface treated metal sheet so as to laminate said copolyester resin film thereto.
15. A method as claimed in claim 14, further comprising adding a lubricant to said copolyester resin film, said lubricant having a particle size below about 2.5 pm.
16. A method as claimed in claim 14 or claim 15, wherein said resin composite is applied to said copolyester resin film in an amount ranging from about 0.1 to about 5.0 g/m2 of said copolyester resin film, said method further comprising drying said applied resin composite at a temperature from about 50 to about 150 C.
17. A method as claimed in claim 16, wherein said resin composite is dried at a temperature from about 60 to about 1500C for from about 5 to about 30 seconds.
18. A method as claimed in any one of claims 14 to 17, wherein said treated metal surface is selected from a tin free steel having double layers of an upper layer of hydrated chromium oxide and a lower layer of metallic chromium, an electrotinplate covered with said double layers, said electrotinplate covered with hydrated chromium oxide and said aluminum treated in a solution containing chromate, phosphate or zirconium salt, heating at a temperature within the melting point of said copolyester resin film +50"C, and rapidly or gradually quenching.
19. A method of preparing a copolyester resin film laminated metal sheet substantially as herein described with reference to the Examples.
20. A copolyester resin film laminated metal sheet when prepared by a method as claimed in any of claims 14 to 19.
21. A container for foods or beverages comprising a copolyester resin film laminated metal sheet as claimed in any of claims 1 to 13.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002000356A CA2000356C (en) | 1989-11-09 | 1989-10-10 | Copolyester resin film laminated metal sheet and method for production thereof |
| FR898914215A FR2653703B1 (en) | 1989-11-09 | 1989-10-30 | LAMINATE METAL SHEET WITH COPOLYESTER RESIN FILM AND PROCESS FOR PRODUCING SAME. |
| GB8925353A GB2238507B (en) | 1989-11-09 | 1989-11-09 | Copolyester resin film laminated metal sheet |
| US07/815,646 US5272011A (en) | 1989-10-11 | 1991-12-30 | Copolyester resin film laminated metal sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8925353A GB2238507B (en) | 1989-11-09 | 1989-11-09 | Copolyester resin film laminated metal sheet |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| GB8925353D0 GB8925353D0 (en) | 1989-12-28 |
| GB2238507A true GB2238507A (en) | 1991-06-05 |
| GB2238507B GB2238507B (en) | 1993-08-25 |
Family
ID=10666017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB8925353A Expired - Lifetime GB2238507B (en) | 1989-10-11 | 1989-11-09 | Copolyester resin film laminated metal sheet |
Country Status (3)
| Country | Link |
|---|---|
| CA (1) | CA2000356C (en) |
| FR (1) | FR2653703B1 (en) |
| GB (1) | GB2238507B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0474240A2 (en) * | 1990-09-06 | 1992-03-11 | Teijin Limited | Polyester film for laminated metal sheet drawing and processing |
| EP0574232A2 (en) * | 1992-06-09 | 1993-12-15 | Teijin Limited | Biaxially oriented polyester film |
| GB2242159B (en) * | 1990-03-19 | 1994-02-02 | Toyo Kohan Co Ltd | Copolyester resin film-metal sheet laminates |
| US5424121A (en) * | 1992-09-06 | 1995-06-13 | Teijin Limited | Biaxially oriented polyester film |
| FR2715344A1 (en) * | 1994-01-19 | 1995-07-28 | Toyo Kohan Co Ltd | Metal sheet laminated with polyester film, useful for food or beverage container |
| WO1997003823A1 (en) * | 1995-07-21 | 1997-02-06 | British Steel Plc | Polymer/metal laminate and method for producing the same |
| GB2309931A (en) * | 1996-02-06 | 1997-08-13 | British Steel Plc | Laminated tin mill products |
| EP0798112A2 (en) * | 1992-07-22 | 1997-10-01 | Teijin Limited | Biaxially oriented laminated polyester film for use as film to be bonded onto metal sheet |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1443109A (en) * | 1973-06-30 | 1976-07-21 | Toyo Boseki | Film having excellent slip characterisitcs and its production |
| GB1495659A (en) * | 1974-12-13 | 1977-12-21 | St Joe Minerals Corp | Superplastic zinc-plastic laminated sheet and method of making same |
| GB1531413A (en) * | 1974-11-04 | 1978-11-08 | Herberts & Co Gmbh | Method for joining foils |
| GB1566422A (en) * | 1975-11-26 | 1980-04-30 | Toray Industries | Coated metal sheet and process for production therefor |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1329723A (en) * | 1970-09-08 | 1973-09-12 | Ici Ltd | Laminated sheets of metals and plastics |
| JPS5230028B2 (en) * | 1973-02-02 | 1977-08-05 | ||
| JPS5610451A (en) * | 1979-07-05 | 1981-02-02 | Toray Industries | Resin coated metallic plate for vessel |
| EP0034781B1 (en) * | 1980-02-21 | 1984-02-01 | BASF Aktiengesellschaft | Process for making ductile laminates |
| JPS5926460A (en) * | 1982-08-06 | 1984-02-10 | 東洋製罐株式会社 | Composite material for packing vessel cover |
| FR2571659B1 (en) * | 1984-10-12 | 1990-11-02 | Toyo Kohan Co Ltd | PROCESS FOR PRODUCING A METAL SHEET COATED WITH A POLYESTER RESIN FILM AND PRODUCT OBTAINED |
| EP0209393B1 (en) * | 1985-07-19 | 1991-05-02 | Toyo Seikan Kaisha Limited | Deep-draw-formed vessel and process for preparation thereof |
| DE3634885A1 (en) * | 1986-10-14 | 1988-04-21 | Hoechst Ag | Composite element |
-
1989
- 1989-10-10 CA CA002000356A patent/CA2000356C/en not_active Expired - Lifetime
- 1989-10-30 FR FR898914215A patent/FR2653703B1/en not_active Expired - Lifetime
- 1989-11-09 GB GB8925353A patent/GB2238507B/en not_active Expired - Lifetime
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1443109A (en) * | 1973-06-30 | 1976-07-21 | Toyo Boseki | Film having excellent slip characterisitcs and its production |
| GB1531413A (en) * | 1974-11-04 | 1978-11-08 | Herberts & Co Gmbh | Method for joining foils |
| GB1495659A (en) * | 1974-12-13 | 1977-12-21 | St Joe Minerals Corp | Superplastic zinc-plastic laminated sheet and method of making same |
| GB1566422A (en) * | 1975-11-26 | 1980-04-30 | Toray Industries | Coated metal sheet and process for production therefor |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2242159B (en) * | 1990-03-19 | 1994-02-02 | Toyo Kohan Co Ltd | Copolyester resin film-metal sheet laminates |
| EP0474240A2 (en) * | 1990-09-06 | 1992-03-11 | Teijin Limited | Polyester film for laminated metal sheet drawing and processing |
| EP0474240A3 (en) * | 1990-09-06 | 1993-01-13 | Teijin Limited | Polyester film for laminated metal sheet drawing and processing |
| US5372867A (en) * | 1990-09-06 | 1994-12-13 | Teijin Limited | Polyester film for laminated metal sheet drawing and processing containing solid lubricant and having specified protrusion rate |
| EP0574232A2 (en) * | 1992-06-09 | 1993-12-15 | Teijin Limited | Biaxially oriented polyester film |
| EP0574232A3 (en) * | 1992-06-09 | 1994-03-16 | Teijin Ltd | |
| EP0798112A2 (en) * | 1992-07-22 | 1997-10-01 | Teijin Limited | Biaxially oriented laminated polyester film for use as film to be bonded onto metal sheet |
| EP0798112A3 (en) * | 1992-07-22 | 1999-10-06 | Teijin Limited | Biaxially oriented laminated polyester film for use as film to be bonded onto metal sheet |
| US5424121A (en) * | 1992-09-06 | 1995-06-13 | Teijin Limited | Biaxially oriented polyester film |
| FR2715344A1 (en) * | 1994-01-19 | 1995-07-28 | Toyo Kohan Co Ltd | Metal sheet laminated with polyester film, useful for food or beverage container |
| NL9400154A (en) * | 1994-01-19 | 1995-09-01 | Toyo Kohan Co Ltd | Metal sheet covered with a polyester resin foil for a deep-drawn look. |
| WO1997003823A1 (en) * | 1995-07-21 | 1997-02-06 | British Steel Plc | Polymer/metal laminate and method for producing the same |
| GB2309931A (en) * | 1996-02-06 | 1997-08-13 | British Steel Plc | Laminated tin mill products |
| EP0791453A2 (en) * | 1996-02-06 | 1997-08-27 | British Steel Corporation | Polymer/metal laminate and process for producing the same |
| EP0791453A3 (en) * | 1996-02-06 | 1998-04-29 | British Steel Corporation | Polymer/metal laminate and process for producing the same |
| GB2309931B (en) * | 1996-02-06 | 1999-07-21 | British Steel Plc | Improvements in and relating to laminated tin mill products and methods of producing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2653703A1 (en) | 1991-05-03 |
| CA2000356A1 (en) | 1991-04-10 |
| FR2653703B1 (en) | 1992-07-24 |
| CA2000356C (en) | 1995-08-22 |
| GB8925353D0 (en) | 1989-12-28 |
| GB2238507B (en) | 1993-08-25 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PE20 | Patent expired after termination of 20 years |
Expiry date: 20091108 |