JP4627147B2 - Manufacturing method and manufacturing apparatus for resin-coated metal seamless can - Google Patents

Description

  The present invention forms a bottomed cylindrical cup body (hereinafter also simply referred to as a cup) from a resin-coated metal plate, and the cup is molded by ironing in a dry state by drawing ironing or ironing. The present invention relates to a method and an apparatus for manufacturing a coated metal seamless can.

  Various seamless cans are used as containers for various beverages and foods. A seamless can is a metal can comprising a can body having no seam on the side surface and a bottom portion formed integrally with the can body without a seam. In particular, a metal material such as an aluminum plate, tin plate or tin-free steel plate is drawn at least once between a drawing die and a punch to form a cup, and then a punch is formed on the cup body. Thinner container body by drawing or squeezing between the dies and the die is used as a highly economical container because the manufacturing cost is low and high-speed production is possible. ing.

  A seamless can manufactured by such drawing ironing or ironing is generally manufactured by the following process. First, a metal plate is punched into a predetermined shape (usually a circle), then formed into a cylindrical cup with a bottom by drawing and then made into a smaller diameter cup by redrawing, and then by ironing. After setting to a predetermined thickness and outer dimensions, the height is adjusted to a predetermined dimension by trimming. The can thus formed is washed and dried, and then is subjected to inner and outer surface coating, outer surface printing and baking, and a neck portion and a flange portion are formed, which are sent to consumers such as beverage manufacturers. During ironing molding, it is necessary to use a large amount of a lubricating fluid (coolant) that also serves as a coolant. Therefore, in the process of cleaning the molded can, a device for degreasing, washing, and chemical conversion treatment and its wastewater treatment equipment are installed. I have.

  On the other hand, by applying a lubricant to the surface of a metal plate whose surface is coated with a thermoplastic resin in advance, ironing is performed in a dry state, and then heated to volatilize and remove the lubricant. The way is done. The seamless can manufactured by this method can omit the degreasing, washing, chemical conversion treatment process and waste water treatment equipment in the production of the conventional seamless can, and the equipment costs, fuel, electricity, water, etc. The cost of sub-materials can be saved significantly. In addition, it can be said that this is a desirable method for making cans in the present age when environmental burdens are small and environmental problems have become a major social problem.

  The manufacturing method of seamless cans performed in such a dry state has been practically successful in making cans at relatively low speeds, but production at high speeds like conventional seamless can manufacturing methods using coolants is possible. It was difficult to apply. In particular, in seamless cans using aluminum or aluminum alloys, friction heat between the can and the die generated during drawing ironing or ironing during canning at high speed, or processing heat generated by deformation of the can The temperature of the can rises due to molding heat, etc., the resin layer softens and scrapes on the outer surface side, a defect called a build-up that causes streak scratches on the surface occurs, and the resin layer softens on the inner surface side As a result, there is a problem in that the punch cannot be pulled out of the can due to welding of the can to the punch or the frictional force between the resin layer on the inner surface of the can and the punch increases, and so-called strip defects frequently occur. In order to prevent these problems, various can manufacturing methods have been proposed.

  Patent Document 1 discloses a method for producing a resin-coated seamless can coated with a thermoplastic resin at a high speed, and maintains the performance of the lubricant while performing punching and ironing as well as a seamless can after ironing. In order to reduce the dynamic friction force of the punch as much as possible, the punch surface temperature is kept between 35 ° C and 100 ° C, and the stripping during the ironing process and seamless stripping that prevents strip defects that occur when the punch is pulled out from the seamless can after the ironing process are prevented. A method for manufacturing a can is described.

  In Patent Document 2, the surface temperature of the die, punch, and punch holder is maintained at a glass transition temperature Tg of the organic coating T + 50 ° C. or lower and appropriately within a temperature range of 10 ° C. or higher. Reduces the coefficient of dynamic friction with the organic coating, prevents breakage due to high frictional resistance, softens the organic coating during molding, and the outer organic coating is scraped off during ironing, Or, when a punch is pulled out from a seamless can, a method for manufacturing a seamless can is described in which an inner surface organic film is in close contact with the punch and prevents the defective punch from being removed from the seamless can after forming.

Patent Document 3 discloses an initial drawing process in which a composite steel sheet obtained by laminating a PET resin layer on one surface of a steel sheet is plastically processed into a cup having a limit drawing ratio or less whose inner surface is the PET resin layer, and the depth of the cup is increased. Is a deep drawing process in which a deep bottom container deeper than the diameter is drawn, and each of the processes is drawn using a punch and a die. In each drawing process, the punch is made of PET as a material to be processed. A method for producing a deep-drawn container is disclosed in which the processability of the resin layer is maintained at a temperature of 50 ° C. to 80 ° C. to prevent damage to the PET resin layer during deep drawing due to overheating.
JP 2002-178049 A JP-A-7-275961 Japanese Patent Laid-Open No. 1-278921

  However, in the method described in Patent Document 1, as a property of the lubricant applied to the surface, there is a property that the dynamic friction coefficient becomes larger as the temperature is lower, and the temperature of the can during molding suitable for molding is 35 ° C to 100 ° C. Since it is limited to the range, it is necessary to heat the punch before molding.

  And since molding heat is generated by ironing molding after the start of molding, it is necessary to cool the punch, but it is necessary to cool the punch after heating once, and to keep the cooling liquid above a certain temperature When applied to high-speed can manufacturing with a large calorific value, it becomes difficult to keep the punch temperature at 35 ° C to 100 ° C. Molding at a temperature exceeding 100 ° C deteriorates the properties of the thermoplastic resin, and the broken body during the ironing process and the organic coating on the outer surface are scraped off to cause streak damage. After the ironing process, the punch is extracted from the seamless can. This causes a problem of so-called strip failure that sometimes occurs. For this reason, it is disadvantageous to increase the molding speed, and it is inferior in economic efficiency from the viewpoint of manufacturing cost.

  Even in the method described in Patent Document 2, it is necessary to maintain the surface temperature of the die, punch, and punch holder in the temperature range of 10 ° C. or more at the glass transition temperature Tg + 50 ° C. or less of the organic coating. It is necessary to maintain the temperature range suitable for molding by starting the cooling after molding is started, and the cooling liquid cannot be set below a certain temperature. There was a problem that the surface temperature of the glass transition temperature Tg + 50 ° C. or less of the coating could not be maintained.

  The method described in Patent Document 3 is a method for producing a container by drawing, and unlike the seamless can made by drawing ironing or ironing, which is the subject of the present invention, the molding speed and the molding heat generated during processing are different. There is a problem in applying to the seamless can targeted by the present invention because it is intended for a small one. In addition, it is necessary to maintain the temperature of the punch in the temperature range of 50 ° C. to 80 ° C., the cooling liquid cannot be kept below a certain temperature, and the cooling effect is low. It is difficult to apply when making cans.

  In the method of manufacturing a resin-coated metal seamless can by drawing or ironing in a dry state, the present invention may cause defects such as streak scratches (build-up) or strip defects generated on the outer surface of the can. It is an object of the present invention to provide a method for producing a seamless can which is capable of producing cans at a high speed (particularly, cans produced at 150 cans / min or more) and is excellent in economy.

That is, in the invention of claim 1, a lubricant is applied to both surfaces of a resin-coated metal plate coated with a resin on at least the outer surface of the can, and the resin-coated metal plate is cut into a disk shape and drawn. A bottomed cylindrical cup body is formed, and a cooling liquid is allowed to flow through the cup body and the die, and the resin-coated metal seamless can is manufactured by ironing or drawing ironing in a dry state. In the manufacturing method of the resin-coated metal seamless can, the punch cooling liquid flow rate Vp and the die cooling liquid flow rate Vd are punch cooled so that the punch heat absorption rate Rp defined by the following formula (1) is 55% or more. The liquid temperature Tp1 when the liquid flows into the punch, the liquid temperature Td1 when the die cooling liquid flows into the die, the liquid temperature Tp2 when the punch cooling liquid flows out from the punch, and the flow of the die cooling liquid from the die Resin-coated metal seamless can which is characterized that you keep the can body side wall temperature Tc2 during ironing by Rukoto be controlled based on the digital liquid temperature Td2 to 80 ° C. below the glass transition point of the resin A manufacturing method is provided.
Formula (1) Rp = Qp / QA × 100 [%]
However, in Formula (1),
QA is the total amount of heat absorbed per unit time during the continuous production of seamless cans defined by equation (2) (hereinafter, simply referred to as total endothermic amount).
Qp is the amount of heat per unit time absorbed by the punch cooling liquid in the seamless can continuous production defined by the equation (3) (hereinafter, simply referred to as punch endotherm).
Formula (2) QA = Qp + Qd + Qc [J / min]
However, in Formula (2),
Qp is the amount of heat per unit time absorbed by the punch cooling liquid in the seamless can continuous production defined by equation (3). Qd is absorbed by the die cooling liquid in the seamless can continuous production defined by equation (4). The amount of heat per unit time (hereinafter, simply referred to as die endothermic amount)
Qc is the amount of heat received by the can per unit time during the seamless can continuous production defined by the equation (5) (hereinafter, simply referred to as the can endotherm).
Formula (3) Qp = (Tp2−Tp1) × cp × sp × Vp [J / min]
However, in Formula (3),
cp: density of punch cooling liquid [g / cm ³ ], sp: specific heat of punch cooling liquid [J / (g · K)]
Tp1 [° C]: Liquid temperature when the punch cooling liquid flows into the punch Tp2 [° C]: Liquid temperature when the punch cooling liquid flows out from the punch Vp: Flow rate of the punch cooling liquid [cm ³ / min]
Formula (4) Qd = (Td2-Td1) * cd * sd * Vd [J / min]
However, in Formula (4),
cd: Density of cooling liquid [g / cm ³ ], sd: Specific heat of dice cooling liquid [J / (g · K)]
Td1 [° C.]: Liquid temperature when flowing into the die Td2 [° C.]: Liquid temperature when flowing out from the die Vd: Flow rate of the die cooling liquid [cm ³ / min]
Formula (5) Qc = (Tc2-Tc1) * cc * sc * Nc [J / min]
However, in Formula (5),
cc: Mass of can barrel side wall [g], sc: Specific heat of can material [J / (g · K)]
Tc1 [° C]: Room temperature Tc2 [° C]: Can barrel side wall temperature during ironing Nc: Number of cans produced per unit time [can / min]

In addition, the manufacturing apparatus according to the present invention includes a resin-coated metal plate that is formed by drawing and forming a resin on at least the outer surface of the can and applying a lubricant on both sides as described in claim 2. In a manufacturing apparatus for a resin-coated metal seamless can, a cup-shaped body is manufactured by ironing or drawing and ironing in a dry state with a punch and a die through which a coolant flows. The amount of heat absorbed per unit time absorbed by the coolant flowing through the punch during continuous production and the amount of heat absorbed per unit time absorbed by the coolant flowing through the die during continuous production. The punch endothermic amount relative to the total amount of heat calculated from the die endothermic amount, which is the amount of heat, and the amount of heat received by the can per unit time during continuous production. Has a punch endothermic ratio calculating means for calculating a slip, the punch wherein such punch endothermic rate is the can body side wall temperature Tc2 during ironing molding with 55% or more 80 ° C. or less which is a glass transition point of the resin And a flow rate control means for controlling the flow rate of the coolant and the flow rate of the coolant of the die.

In the method and apparatus of the present invention, the punch and die used for drawing ironing or ironing are cooled by the cooling liquid flowing through the inside, and the punch heat absorption amount Qp absorbed by the punch cooling liquid is the punch cooling liquid. The flow rate Vp of the punch cooling liquid and the flow rate Vp of the die cooling liquid when the punch cooling liquid flows into the punch so that the total endothermic amount QA of the endothermic heat by the die cooling liquid and the seamless can is 55% or more. Control is based on the liquid temperature Tp1 of the die cooling liquid, the liquid temperature Td1 when the die cooling liquid flows into the die, the liquid temperature Tp2 when the punch cooling liquid flows out from the punch, and the liquid temperature Td2 when the die cooling liquid flows out from the die. Since the can is cooled so that the temperature Tc2 of the can body side wall at the time of ironing becomes 80 ° C. or less, which is the glass transition point of the resin coating the outer surface of the can , Providing a seamless can ironing method that can prevent high-speed can manufacturing by preventing defects such as streaks (build-up) and strip defects that occur on the outer surface of the can. Can do. In particular, when making cans at a high speed with the number of cans Nc of 150 [cans / min.] Or when the temperature of the side wall of the can body during ironing is Tc2 of 45 ° C or more, cooling by punching is promoted. Thus, it is possible to effectively prevent defects such as streak (build-up) and strip defects that occur on the outer surface of the can.

  Further, in the apparatus according to claim 2, seamless cans can be manufactured in an optimum state corresponding to manufacturing conditions such as can body size, can material, environmental temperature, and can manufacturing speed. That is, the punch heat absorption rate required for various manufacturing conditions is set, and by controlling the flow rate of the coolant so that it exceeds the set punch heat absorption rate, seamless cans can be manufactured satisfactorily. become. This is particularly effective in the case of high-speed can manufacturing with a large calorific value.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a cross-sectional view showing an example of a resin-coated metal plate used in the present invention, FIG. 2 is a cross-sectional view of a bottomed cylindrical cup, and FIG. 3 is a cross-sectional view of a seamless can formed by the forming method of the present invention. is there.

  FIG. 4 is an explanatory diagram schematically showing the overall configuration including the control system of the manufacturing apparatus according to the present invention, and FIG. 5 is a sectional view of the ironing punch used in the present invention.

  First, the metal used for the resin-coated metal plate 1 shown in FIG. 1 may be any metal used for canning, and various surface-treated steel plates, aluminum alloy plates, and the like are used. For example, as the surface-treated steel sheet, it is possible to use one or a plurality of surface treatments such as zinc plating, tin plating, nickel plating, electrolytic chromic acid treatment, chromic acid treatment, and the like as an aluminum alloy. Is preferably a JIS 3004 aluminum alloy or the like. Moreover, it is preferable to provide a chemical conversion treatment film also on the surface of an aluminum alloy plate. This is to improve the adhesion between the resin layer and the surface of the metal plate so that the resin layer formed on the upper layer does not peel even when it is molded. The types of chemical conversion coatings include general alkali-chromate-based, chromate-based, chromium phosphate-based, zinc phosphate-based, coated chromate-based, zirconium phosphate-based, and titanium phosphate. In addition, a phosphoric acid water-soluble resin system or the like can be used as appropriate. Among these, in consideration of various properties required for the metal plate in the present invention, particularly adhesion and productivity, a chromate film by phosphoric acid chromate treatment is preferable. This chromate film can be applied by a known method, but can be suitably coated by a dipping method or a spray method.

When a chromate film is used as the chemical conversion film, the coating amount on the surface of the metal plate is preferably 10 to 30 mg / m ² by dry weight. When the coating amount is less than 10 mg / m ^{2 in} terms of Cr amount, the chromate film on the plate surface becomes non-uniform, and the effect of improving the adhesion between the thermosetting resin layer and the metal plate surface is lost. On the other hand, if the coating amount exceeds 30 mg / m ^{2 in} terms of Cr amount, cracking is likely to occur in the chromate film at the time of ironing molding and the adhesion is deteriorated.

  Next, a resin layer is provided on at least the surface of the metal plate 1 that is the outer surface of the can. The resin used in the present invention is not particularly limited as long as it is usually used in the production of cans, and a known thermoplastic resin or thermosetting resin is used.

  When the resin layers are provided on both surfaces of the metal plate 1, the metal plate and the punch are not in direct contact at the time of drawing ironing or ironing, and the life of the punch and the die is extended. In addition, since the resin layer is also formed on the inner surface side of the can, it is possible to reduce the application amount in the step of applying the inner surface coating applied in a later step or to eliminate the step of applying the inner surface coating itself.

  When a thermoplastic resin is used as the resin for forming the resin layer on the metal plate 1, a thermoplastic polyester resin is preferably used particularly from the viewpoint of heat resistance and content resistance.

  As a method for forming a thermoplastic resin layer on a metal plate, a resin layer is formed by extruding a molten resin onto the surface of the metal plate, or a resin film is formed in advance, and the film is then bonded to the metal by an adhesive or heat fusion. A known method such as a method of forming a resin layer by sticking to a plate can be appropriately used.

  In terms of ironing workability, the formed resin layer is preferably amorphous. As a method for obtaining this amorphous resin-coated metal thin plate, a resin film formed in advance is supplied on the surface of a heated metal plate, laminated by thermocompression bonding between rolls, and immediately cooled immediately to make the resin amorphous. And a method of extruding molten resin on the surface of the metal plate and laminating and quenching, a method of once heating the metal plate laminated with a crystalline resin above the melting point of the resin, and quenching. It is also possible to adhere a resin film prepared in advance by a known method to a metal plate with an adhesive. As the adhesive, a polyester resin or an epoxy resin can be selected as appropriate.

  When a thermosetting resin is used as the resin for forming the resin layer on the metal plate 1, a thermosetting polyester resin is preferably used. As the thermosetting polyester resin, modified polyester resins such as epoxy-modified and urethane-modified can also be suitably used. The thermosetting polyester resin is a polyester resin having an unsaturated bond, and is obtained by binding an acid component containing an unsaturated acid and an alcohol at least partially.

  As the curing agent to be added to the thermosetting resin, a known one can be used, but it is preferable to use an amino resin or a melamine resin because of excellent workability. In particular, when used as a food container, it is preferable to use a phenol resin for the inner surface. It is because elution of formalin to the contents can be prevented by using a phenol resin.

  Moreover, it is preferable to contain 3 mass% or less of lubricating components with respect to a thermosetting resin in a thermosetting resin layer. In the present invention, by setting the punch heat absorption rate Rp to 55% or more, molding can be performed at a temperature lower than the temperature at which the resin softens, and a seamless can can be manufactured at high speed even with a lubricating component of 3% by mass or less. Yes. A more preferable content of the lubricating component is 0.5% by mass to 1.0% by mass with respect to the thermosetting resin. If the content of the lubricating component exceeds 3% by mass, the adhesion of the ink at the time of printing on the outer surface is inferior, and the printing on the outer surface may be peeled off. On the inner surface, when the inner surface coating that protects the inner surface of the container is applied on the thermosetting resin layer for the seamless can after molding, the coating is repelled and the adhesion is deteriorated, resulting in a decrease in the inner surface quality. There is. Further, the melting point of the lubricating component contained in the thermosetting resin needs to be equal to or lower than the baking temperature of the thermosetting resin. If the melting point exceeds the baking temperature, the lubricating component does not melt in the baking process of the thermosetting resin, it remains in the resin in the form of particles, and the adhesion of the ink when printing on the outer surface is poor. This is because printing may be peeled off or streaks on the surface (build-up) may be caused. More preferably, a lubricating component having a melting point of 80 ° C. or lower is used. A vegetable oil having a melting point of 0 ° C. or lower such as oleic acid and linoleic acid is more preferable. The lower the melting point of the lubricating component, the better the adhesion of the printing ink when printing is performed on the outer surface of the molded seamless can, so there will be no peeling of the print, and the inner surface of the molded seamless can In the case of applying an inner surface protective paint for protecting the surface, it is possible to produce a seamless can having good adhesion of the inner surface protective paint and good inner surface quality.

  In the case of forming a thin resin layer, when a thermosetting resin is used, the thickness of the resin layer formed on the surface of the metal plate is made thinner than when the resin layer is formed of a thermoplastic resin. This is advantageous. The thinner the resin layer, the less the amount of resin to be used, and the more economical the resin can be applied to the metal plate. In addition, in high-speed can manufacturing, the thinner the resin layer formed on the surface of the metal plate, there is an effect that build-up is less likely to occur.

  When a thermoplastic resin is used, in a known method, the thickness of the resin layer is effective for preventing streak damage (build-up) generated on the outer surface of the can in a high-speed can of 150 cans / minute or more. It is difficult to obtain a thickness of 7 μm or less. That is, in order to obtain a thermoplastic resin layer having a thickness of 7 μm or less, a method of forming a resin layer by attaching a thermoplastic resin film having a thickness of 7 μm or less to a metal plate is preferably used. In order to prevent breakage at the time of sticking, the speed of sticking must be greatly reduced as compared with a normal case, and the tension of the film must be precisely controlled. However, it becomes easy to reduce the thickness of the resin layer to 7 μm or less by using the thermosetting resin. This is because the thermosetting resin has a relatively low viscosity and can be applied to the surface of the metal plate and baked. When the thermosetting resin is used in the present invention, the viscosity before baking is preferably 10 seconds to 50 seconds, more preferably 10 seconds to 30 seconds (both are Ford Cup No. 4/25 ° C.). When the viscosity is high, it may be applied by diluting with a solvent in order to adjust the viscosity. However, in consideration of workability, cost, economy, etc., it is preferable to apply the raw solution without using a solvent.

  This thermosetting resin layer is preferably formed on the inner surface side so that the thickness of the resin layer is 1 μm to 11 μm. If the thickness of the thermosetting resin layer is less than 1 μm, the resin layer is too thin and the metal surface may be exposed after ironing. If it is greater than 11 μm, the amount of resin applied necessary for forming the resin layer In addition, since the coating speed becomes slower, the economy is inferior.

  In addition, on the outer surface side, the resin layer is preferably formed to have a thickness of 1 μm to 7 μm. When the thickness of the thermosetting resin layer is less than 1 μm, the resin layer on the surface is too thin, and the metal surface may be exposed after ironing, as in the case of the inner surface. The thickness of the resin layer exceeds 7 μm. And there is a problem that streaks (build-up) occurs. Moreover, when the performance and economical efficiency of the resin layer are taken into consideration, the more preferable film thickness is 1.5 μm to 4 μm on both the inner and outer surface sides.

  In applying the thermosetting resin to the metal plate 1, it can be applied by a known method such as coating by a roll coater. The metal plate coated with the thermosetting resin is appropriately heated to a baking temperature by a known method such as hot air drying, infrared heating, induction heating, etc., and the resin is baked on the metal plate to form a thermosetting resin layer. The The baking temperature is preferably 260 ° C. or higher and 272 ° C. or lower as the plate temperature. If the temperature is lower than 260 ° C., the resin is not sufficiently cured, and if the temperature exceeds 272 ° C., the resin is excessively baked to be in a so-called overbaked state, and the properties of the resin are deteriorated. This can cause defects on the inner and outer surfaces of the can. The baking time can be appropriately set in consideration of the resin composition, the required performance of the resin layer, and the like, but it is preferably a short time in consideration of economy. Specifically, it is set to about 15 to 40 seconds.

A lubricant is applied to both surfaces of the resin-coated metal plate 1 thus prepared. When the contents of the container are foods and beverages, it is preferable to use a lubricant that does not have any food hygiene problems, such as normal butyl stearate, liquid paraffin, petrolatum, white petrolatum or the like. In the case of these lubricants, 30 mg / ^{m 2} or more to 150 mg / ^{m 2} or less of the coating amount as the coated amount of oil one side practically preferable. If the coating amount is less than 30 mg / m ² , the coating amount is too small and the lubricating effect is small and impractical. When the coating amount is larger than 150 mg / m ² , the effect is saturated, which is not economical. As the application method, a known method such as application by spraying, application using a roll or a gravure roll can be appropriately used. Considering the workability of coating, it is preferable to use a liquid lubricant at normal temperature.

  The resin-coated metal plate 1 coated with a lubricant is cut into a disk shape, and a bottomed cylindrical cup 4 as shown in FIG. 2 is formed by drawing. If necessary, a cup having a predetermined shape is formed by drawing a plurality of times.

  The cup 4 formed in this way is subjected to drawing ironing or ironing to produce a resin-coated metal seamless can 5 as shown in FIG. FIG. 4 shows a main part of the ironing apparatus. In the ironing apparatus, the ironing dies 7 of one or a plurality of pieces (first to third dies 7a, 7b, 7c in the figure) have the same axis as the central axis of the ironing punch 6. Are arranged as follows. The punch 6 is disposed so as to be able to move forward and backward so as to pass through the die 7, and moves between the most retreating top dead center and the most advanced bottom dead center to iron the can. A stripper device (not shown) is provided on the bottom dead center side of the third die 7c to extract the punch from the seamless can formed by ironing, and the bottom of the can is formed near the bottom dead center of the punch 6. A bottom molding device (not shown) is arranged.

  The cup 4 that is supplied near the top dead center and is held so as to cover the tip of the punch 6 is inserted into the die 7 so that the cup side wall portion is ironed to reduce the thickness, and the predetermined wall thickness and shape are reduced. The seamless can 5 is ironed.

  In the seamless can manufacturing method of the present invention, a seamless can is manufactured in a dry state without spraying coolant (cooling lubricant) during ironing. Therefore, a method is used in which the cooling liquid flows through the inside of the punch and the die so that the can surface temperature is kept at the glass transition point of the resin + 30 ° C. or lower, preferably 80 ° C. or lower. Generally, the resin used for the resin-coated metal seamless can starts to soften at a temperature near the glass transition point, and the softening of the resin proceeds as the temperature increases. When the temperature exceeds the glass transition point + 30 ° C., the can is softened to such an extent that a defect occurs. In addition, as the can-making speed increases, the load that the can receives during molding increases, and the resin coating is required to be more sound, and it is necessary to make cans at a lower temperature. Considering the temperature range of the glass transition point of thermoplastic polyester and thermosetting polyester, which are currently widely used as materials for seamless cans, the can temperature is 80 ° C or less when drawing or ironing at high speed. It is desirable to keep In the present invention, there is provided a method for producing a seamless can capable of keeping the can temperature at 80 ° C. or lower even in high-speed can making. Below, the cooling means of this invention is demonstrated.

  A punch used in the present invention is shown in FIG. The punch 6 includes a support cylinder 8 and a sleeve 9, and a flow path 10 is formed between the support cylinder 8 and the sleeve 9 for allowing the coolant to flow therethrough. The cooling liquid supplied from the cooling liquid supply device 13 a flows into the spiral flow path 10 formed between the support cylinder 8 and the sleeve 9 from the inflow path 11 formed on the base side of the support cylinder 8. After reaching the distal end along the flow path 10, the spiral passage 10 ′ formed from the distal end toward the root reaches the root of the punch 6 and reaches the root of the support cylinder 8 of the punch 6. It flows out of the punch 6 through the outflow passage 12 formed on the side. That is, as shown in FIG. 5, a double spiral groove is formed on the surface of the support cylinder 8 of the punch 6 so as to be the coolant flow paths 10 and 10 ′ when fitted into the sleeve 9. Yes. That is, the spiral flow path 10 in which the cooling liquid flows from the root side to the tip end of the punch 6 and the spiral flow path 10 ′ in which the cooling liquid flows from the tip end toward the root side form a double helix. Yes. By configuring the spiral flow paths 10 and 10 'as described above, the punch 6 is uniformly cooled, so that the surface temperature does not vary and good molding is possible. In particular, in ironing molding at a high speed exceeding 150 cans / minute, the resin layer is softened in the high temperature portion formed by uneven temperature on the punch surface than in the low temperature portion. This is effective because it is possible to prevent the processing force acting on the surface of the resin layer from fluctuating and the resin layer from being scraped to easily cause streak (build-up).

  The coolant that has flowed out is returned to the coolant supply device 13a again through the piping, the temperature of the coolant is lowered to a predetermined temperature, and a circulation path that is supplied to the punch again is formed. In the middle of the supply path from the coolant supply device 13a to the punch 6, a booster device 14 for increasing the coolant pressure is disposed in order to increase the coolant flow rate. Moreover, the 2nd cooling fluid supply apparatus 13b for supplying the cooling fluid of temperature different from the cooling fluid supply apparatus 13a can also be installed as needed. When the punch temperature is too low with respect to a preset temperature at the start of molding, a coolant having a temperature higher than the coolant supplied from the coolant supply device 13a is supplied from the second coolant supply device 13b to punch By maintaining 6 at a predetermined temperature, the occurrence of defective cans at the start of molding can be controlled. In that case, a switching device 15 is installed in the piping path so that the supply of the coolant having different temperatures can be switched based on the punch temperature.

  Next, the die used in the method for producing a seamless can of the present invention will be described. A flow path 16 for allowing the coolant to flow therethrough is formed in a substantially annular shape inside the die 7, and the coolant supplied from the coolant supply device 17 at a predetermined temperature passes through the inflow path into the die 7. It passes through the inside of the die 7 through the flow path 16, flows out of the die 7 from the outflow path, is returned to the coolant supply device 17 through the piping path, adjusted to a predetermined temperature, and supplied to the die 7 again. A circulation path is formed. A flow control valve 18 is arranged in the middle of the supply path to the die 7 in order to control the flow rate of the coolant. The temperature of the die cooling liquid is preferably set to a temperature higher than the melting point of the lubricant applied to the surface of the resin-coated metal plate. If the temperature of the die coolant is below the melting point, at the start of seamless can production. This is because the die 7 becomes below the melting point of the lubricant, and the solidified lubricant accumulates on the die 7 and adheres to the molded seamless can, or may cause molding failure.

  Next, the liquid temperature Tp1 when the punch cooling liquid flows into the punch, the liquid temperature Td1 when the die cooling liquid flows into the die, the liquid temperature Tp2 when the punch cooling liquid flows out from the punch, and the die cooling liquid from the die Control of the punch cooling liquid flow rate Vp and the die cooling liquid flow rate Vd based on the liquid temperature Td2 at the time of outflow will be described. The heat generated by the ironing process is absorbed by the punch, the die and the can, respectively, and raises the temperature. In the present invention, the cooling liquid flows through the inside of the punch and the die to absorb the heat so that the molding heat generated during molding is not absorbed by the can and the can temperature rises, and the punch heat absorption amount Qp is the punch heat absorption amount Qp. (The amount of heat per unit time absorbed by the punch cooling liquid) and the die endothermic amount Qd (The amount of heat absorbed per unit time by the die cooling liquid) and the can endothermic amount Qc (The amount of heat received by the can per unit time) The main feature is that the total heat absorption QA (the amount of heat absorbed per unit time during continuous production) is 55% or more.

  Molding heat generated during ironing is mainly generated by frictional heat generated by friction between the die and the can and processing heat generated by deformation of the can due to ironing, but the contact area between the die and the can during molding is very large. Therefore, the amount of heat transferred to the die is also small. On the other hand, the punch has a large contact area with the can, and it is an effective means to increase the amount of heat absorbed from the punch in order to suppress the temperature rise of the can. In the present invention, by making the ratio of the punch endothermic quantity Qp to the total total endothermic quantity QA 55% or more, even in high-speed can manufacturing, the can surface temperature does not exceed 80 ° C. Is possible. When seamless cans are manufactured without spraying coolant (cooling lubricant) during ironing, the temperature of the surface of the cans during continuous cans is produced in conventional canning methods at high speeds exceeding 150 cans / minute. However, in the present invention, the temperature of the surface of the can in continuous cans can be kept at 80 ° C. or lower, and it becomes possible to produce seamless cans that are favorable in terms of economy and quality. .

As shown in FIG. 4, the control unit C measures the temperature of the coolant when flowing into the die and punch and the temperature when flowing out of the die and punch, respectively, and the difference between the flow rate of the coolant per unit time and Multiplying the density and specific heat to calculate the punch endothermic amount Qp and the die endothermic amount Qd from the following formulas (3) and (4), and the temperature of the can body at the time of ironing molding is measured. An arithmetic means (S2) is provided for calculating the difference in the can body heat absorption amount Qc from the following equation (5) by calculating the difference and multiplying the difference by the mass of the can, the specific heat, and the number of cans produced per unit time. A signal based on the value calculated by the calculation means (S1, S2) is sent to a calculation means (S3) for calculating a punch heat absorption rate Rp described later. Here, the specific heat and density of the cooling liquid in the case of obtaining the endothermic amount are determined by the liquid used. For example, when water is used as the coolant used in the present invention, the value varies strictly depending on the water temperature, but the specific heat is 4.2 [J / (g · K)] and the density is 1 [g / cm ^3. ] Can be used to calculate the endothermic amount.

Qp = (Tp2-Tp1) * cp * sp * Vp [J / min] (3)
However,
cp: density of punch cooling liquid [g / cm ³ ], sp: specific heat of punch cooling liquid [J / (g · K)]
Tp1 [° C.]: Liquid temperature when flowing into the punch Tp2 [° C]: Liquid temperature when flowing out from the punch Vp: Flow rate of punch cooling liquid [cm ³ / min]

Qd = (Td2-Td1) * cd * sd * Vd [J / min] (4)
However,
cd: Density of cooling liquid [g / cm ³ ], sd: Specific heat of dice cooling liquid [J / (g · K)]
Td1 [° C.]: Liquid temperature when flowing into the die Td2 [° C.]: Liquid temperature when flowing out from the die Vd: Flow rate of the die cooling liquid [cm ³ / min]

Qc = (Tc2-Tc1) * cc * sc * Nc [J / min] (5)
However,
cc: Mass of can barrel side wall [g], sc: Specific heat of can material [J / (g · K)]
Tc1 [° C]: Room temperature Tc2 [° C]: Can barrel side wall temperature during ironing molding Nc: Number of cans per unit time [can / min]

  Here, in determining the endothermic amount Qc of the can, the mass of the can barrel side wall is used, and the mass of the can bottom is excluded. This is because the temperature rises only at the side wall of the can body that is subjected to ironing, and the bottom of the can is not subjected to ironing, and the can (can body) is subjected to ironing. This is because the temperature at the bottom of the can hardly rises due to heat conduction from the can body. Strictly speaking, the specific heat of the can material is a value determined by the material to be used. For example, when a steel-based material is used, 0.46 [J / (g · K)], an aluminum-based material is used. When used, the endothermic amount can be calculated as 0.9 [J / (g · K)].

  In the present invention, the control unit C includes calculation means (S3) for calculating the punch heat absorption rate Rp expressed by the following formula (1) based on the signal sent from the calculation means (S1, S2). A signal based on the value calculated by the calculation means (S3) is sent to the flow rate control means (S4, S5) described later. Then, the coolant flow rates of the punch and the die are controlled so that the ratio of the endothermic amount Qp of the punch to the total endothermic amount QA expressed by the following formula (2) is 55% or more.

Rp = Qp / QA × 100 [%] (1)
However, in Formula (1),
QA is the total endothermic amount per unit time during continuous production of seamless cans defined by equation (2) QA = Qp + Qd + Qc (2)

  That is, as shown in the above equations (3) and (4), the punch endothermic amount Qp and the die endothermic amount Qd are the differences between the inflow side temperatures Tp1, Td1 and the outflow side temperatures Tp2, Td2, respectively. Since these are proportional to the flow rates Vp and Vd, the flow rates Vp and Vd are controlled based on these temperatures Tp1, Td1, Tp2 and Td2. In this case, if the temperatures Tp1 and Td1 on the inflow side of each coolant are known temperatures set in advance, the temperatures Tp2 and Td2 on the outflow side are substantially detected, and the flow rate Vp is based on the detected values. , Vd are controlled.

  When a metal seamless can having a diameter of about 66 mm, which is generally used as a beverage can, is produced at a high speed of 150 cans / minute or more, a more preferable range of the punch heat absorption rate Rp is 60% to 75%. If it is less than 60%, there may be slight surface roughness depending on the production conditions, although it is at a level that does not cause any practical problems. Further, if it exceeds 75%, there is no problem in quality, but since it is necessary to increase the endothermic amount of the punch, it is necessary to increase the flow rate and the system operation costs and the effect is saturated. Absent.

  The temperature of the punch and die cooling liquid is preferably 5 ° C. or higher and 30 ° C. or lower. If the temperature is lower than 5 ° C., the cooling liquid may freeze in the piping when the temperature drops in winter or the like. Further, at a temperature higher than 30 ° C., the temperature difference from the punch surface or the die surface becomes small and the endothermic amount becomes small, so that a sufficient endothermic effect cannot be obtained. When using the coolant whose temperature is controlled in this way, the temperatures Tp2 and Td2 on the outflow side are detected, and the flow rates Vp and Vd are controlled by the flow rate control means based on the detected values.

  The coolant flow rate control means (S4, S5), when the structure of the flow path through which each coolant flows is determined, executes the control by adjusting the pressure. For example, the flow rate can be controlled by changing the pressure applied by the booster 14 described above. Further, when the pressure applied by the pressurizing source of each coolant is constant, the flow rate may be controlled by changing the opening of the pressure reducing valve or the throttle valve. Furthermore, the control can be performed electrically by using an electronic control unit mainly composed of a microprocessor and an appropriate actuator that operates in response to a command signal from the electronic control unit.

The present invention is suitable for cooling at the time of high-speed can production of 150 [can / min] or more, or suitable for cooling at the time of can making in which the temperature of the side wall of the can body at the time of ironing is 45 ° C. or more. is there. As an example when the temperature of the can body side wall becomes 45 ° C. or more, in addition to the case where the can-making speed is increased, the case where the ironing rate is high, or the case where a seamless can with a high can body is formed, The case where generation | occurrence | production of shaping | molding heat is large, such as when the punch stroke at the time of ironing shaping | molding is long, is mentioned. When the temperature of each cooling liquid is set to 5 ° C. or more and 30 ° C. or less as described above, the preferred range for the flow rate and pressure of the punch cooling liquid varies depending on the speed of the can, but it is drawn or ironed. In molding, from the viewpoint of high-speed can manufacturing, the coolant flow rate Vp is 4 × 10 ³ [cm ³ / min] (4 liters / min) or more, and the coolant pressure is 490 [kPa] (5 kgf / cm). ² ) or more. When the flow rate and pressure are smaller than these values, a sufficient endothermic amount cannot be obtained when cans are produced at high speed, particularly in high-speed cans of 150 [can / min] or more. More preferably, the flow rate Vp is 10 × 10 ³ [cm ³ / min] (10 liters / min) or more, and the coolant pressure is 980 [kPa] (10 kgf / cm ² ) or more.

The preferable range of the flow rate and pressure of the die cooling liquid is that the heat flow to the die during continuous can making is smaller than that of the punch, so the flow rate Vd of the cooling liquid is 2 × 10 ³ [cm ³ / min] (2 Liter / minute) to -8 × 10 ³ [cm ³ / minute] (8 liter / minute) or less, and the coolant pressure is 98 kPa (1 kgf / cm ² ) to 490 [kPa] (5 kgf / cm). ² ). When the flow rate and pressure of the die cooling liquid are below the lower limit of these ranges, a sufficient endothermic amount cannot be obtained. Further, when the flow rate and pressure of the die cooling liquid exceed the upper limit of these ranges, the endothermic effect is saturated, which is not economical.

  The seamless can 5 subjected to ironing is removed from the punch 6 by a stripper device when the punch is pulled back, and the seamless can 5 is formed as shown in FIG. The seamless can 5 formed by ironing is transported to the next process, where appropriate processing such as inner surface coating, outer surface printing / painting, neck / flange molding is performed to produce a final product.

(Experimental example 1)
For the aluminum alloy plate (3004 alloy tempered H19 plate thickness 0.265 mm) treated with phosphate chromate, a thermosetting polyester resin is used as the resin, and the resin layer thickness is 3 μm on both sides of the aluminum alloy plate. A thermosetting resin polyester resin was applied by a roll coater, and the baking conditions were set to a plate temperature of 260 ° C. and a baking time of 20 seconds to prepare a sample.

  The used thermosetting resin for the inner surface of the can is a mixture of a polyester resin having a glass transition point Tg of 80 ° C. and an average molecular weight of 20000 and a polyester resin having an average molecular weight of 15,000 and a glass transition point Tg of 30 ° C. Is used as a base, 4% by mass of a phenol resin is added to the base as a curing agent, and linoleic acid (melting point 0 ° C. or lower) is used as a lubricating component mixed in the thermosetting resin. 1.5% by mass was mixed.

  As the thermosetting resin for the outer surface of the can, a polyester having a glass transition point Tg of 80 ° C. and an average molecular weight of 20,000 was used as a base, and a resin obtained by adding 4% by mass of an amino resin to the base as a curing agent was used. . Further, linoleic acid (melting point: 0 ° C. or lower) as a lubricating component added to the thermosetting resin was mixed with 1.5% by mass with respect to the thermosetting resin.

As a lubricant, normal butyl stearate was applied to both surfaces of the resin-coated aluminum plate by gravure coating as a coating amount of 100 mg / m ^{2 on} both surfaces.

  The aluminum alloy plate coated with the lubricant was cut into a disk having a diameter of 146 mm, a cup having a diameter of 90 mm was formed by the first drawing, and a cup having a diameter of 66.3 mm was formed by the second drawing. The molding speed of cup molding was 140 cans / minute.

The molding machine that performs ironing on the cup is provided with equipment for cooling liquid flowing through the punch and the die as cooling equipment for cooling the punch and the die. Industrial water was used as the cooling liquid, and the cooling liquid was cooled by a cooler so that the temperature Tp1 at the time of inflow of the punch cooling liquid was supplied at 10 ° C. The settings of the water pressure and the flow rate Vp of the punch cooling liquid were controlled to be the values shown in Table 1, respectively. The dice were controlled so that a coolant having a flow rate Vd of 5 × 10 ³ cm ³ / min, a water pressure of 98 kPa (1 kgf / cm ² ), and a water temperature of 30 ° C. was supplied.

  In the ironing machine, as shown in FIG. 4, three ironing dies 7 are arranged so as to have the same axis as the central axis of the ironing punch 6.

The cup 4 supplied to the ironing machine near the top dead center of the punch is inserted into the die while being held so as to cover the tip of the punch, and the side wall is ironed to have an outer diameter of 66 mm and a high height. The thickness was set to 127 mm and the side wall was processed to a thickness of about 105 μm. The forming speed of ironing was set to 300 cans / minute. The ironing ratio with respect to the original plate thickness was 60%, and the mass of the side wall portion of the formed seamless can was 9 g on average. When the cooling liquid and can temperature during molding reach a steady state, measure the temperature difference between the inflow and outflow temperatures of the punch and die cooling liquid, determine the temperature difference, and measure the can temperature immediately after ironing. The specific heat of (aluminum) was set to 0.9 J / (g · K) [0.2 cal / (g · K)], the endothermic amount was calculated, and the endothermic rate Rp by the punch coolant was obtained. As for the water temperature of the cooling liquid, thermocouples were inserted into the inflow and outflow pipes, and the water temperature during molding was measured. About the can temperature, the surface temperature of the can immediately after passing the dice 7c was measured with the infrared sensor. The room temperature at the time of can-making was 20 ° C. The results of evaluating the moldability are shown in Table 1.

  In Examples 1 to 5 in which the heat absorption rate Rp of the punch is 55% or more, the inner and outer surfaces of the can are not peeled off, or the light surface is slightly roughened, and cans can be produced without any practical problems. is there. On the other hand, in Comparative Example 1 in which the punch heat absorption rate Rp was less than 55%, the can surface temperature exceeded 80 ° C., and deep streak peeling occurred.

(Experimental example 2)
The pressure of the punch cooling liquid is 1960 kPa (20 kgf / cm ² ), the flow rate Vp is 16 × 10 ³ cm ³ / min, the room temperature is 10 ° C., the liquid temperature Tp1 when the punch cooling liquid flows into the punch, and the die cooling liquid The liquid temperature Td1 at the time of flowing into the dies was controlled to the temperatures shown in Table 2, and the other conditions were the same as in Experimental Example 1, and seamless cans were prepared to evaluate the moldability. The results are shown in Table 2.

  In Examples 6 to 9, the can temperature was kept at 80 ° C. or less, the punch heat absorption rate Rp was 55% or more, and all had good moldability. On the other hand, in Comparative Example 2, the can temperature exceeded 80 ° C., the punch heat absorption rate Rp was also less than 55%, and streaky peeling occurred on the inner and outer surfaces of the can.

(Experimental example 3)
In Examples 10 to 13 of the present invention, the can-making speed was 150 [can / min], 200 [can / min], 250 [can / min], 300 [can / min], and the punch heat absorption rate Rp was 55%. For Comparative Examples 3 and 4 which are less than 100, the canning speed was set to 100 [can / min] and 200 [can / min], and the influence of the canning speed was examined. The other conditions were the same as in Experimental Example 2 above. Table 3 shows the evaluation results.

  In Comparative Example 3, since the can-making speed was as low as 100 [can / min], even if the punch heat absorption rate Rp was less than 55%, the can temperature did not increase so much and the moldability was good. In Comparative Example 4 where the can-making speed was 200 [can / min], the punch heat absorption rate Rp was below 55%, the can temperature exceeded 80 ° C., and good molding could not be performed.

  As mentioned above, although this invention was demonstrated using the Example, this invention is not limited to these Examples, Appropriate to the said Example, without deviating from description of the claim of this invention. Changes can be made.

It is an enlarged view which shows the cross section of the resin coating metal plate used by this invention. It is a figure which shows the cross section of the cup shape | molded from the resin coating metal plate. It is a figure which shows the cross section of the seamless can shape | molded by the ironing method of this invention. It is explanatory drawing which shows typically the whole structure containing the control system of the manufacturing apparatus which concerns on this invention. It is a schematic diagram which shows the direction of the flow of the punch for ironing shaping | molding used for the ironing shaping | molding method of this invention, and a cooling fluid.

Explanation of symbols

  DESCRIPTION OF SYMBOLS 1 ... Resin coated metal plate, 2 ... Metal plate, 3 ... Resin layer, 4 ... Cup, 5 ... Seamless can, 6 ... Punch, 7, 7a, 7b, 7c ... Dies, 8 ... Supporting cylinder, 9 ... Sleeve, 10 DESCRIPTION OF SYMBOLS ... Punch cooling liquid flow path, 11 ... Inflow path, 12 ... Outflow path, 13a ... Punch cooling liquid supply apparatus, 13b ... 2nd punch cooling liquid supply apparatus, 14 ... Punch cooling liquid pressurization apparatus, 15 ... Punch cooling liquid switching Device: 17 ... Die coolant supply device, C ... Control unit, S1 ... Calculation means (of the amount of heat absorbed per unit time of each coolant of the punch and die), S2 ... (Amount of heat received by the can per unit time) S3... S3... (Calculates the punch heat absorption rate) S4, S5.

Claims (2)

Apply a lubricant to both sides of the resin-coated metal plate with the resin coated on at least the outer surface of the can, cut the resin-coated metal plate into a disk shape, and draw-mold it to form a bottomed cylindrical cup body. In a method for producing a resin-coated metal seamless can, the cup body is made to flow through a cooling liquid in a punch and a die, and a resin-coated metal seamless can is produced by ironing or drawing ironing in a dry state. ,
The punch cooling liquid flow rate Vp and the die cooling liquid flow rate Vd are set so that the punch heat absorption rate Rp defined by the following equation (1) is 55% or more, and the liquid temperature Tp1 when the punch cooling liquid flows into the punch. Ironing by controlling based on the liquid temperature Td1 when the die cooling liquid flows into the die, the liquid temperature Tp2 when the punch cooling liquid flows out from the punch, and the liquid temperature Td2 when the die cooling liquid flows out from the die. the method for producing a resin-coated metal seamless can the can body side wall temperature Tc2 characterized that you keep 80 ° C. below the glass transition point of the resin at the time.
Formula (1) Rp = Qp / QA × 100 [%]
However, in Formula (1),
QA is the total amount of heat absorbed per unit time during the continuous production of seamless cans defined by equation (2) Qp is the unit absorbed by the punch cooling liquid during seamless cans defined by equation (3) Calorie formula per time (2) QA = Qp + Qd + Qc [J / min]
However, in Formula (2),
Qp is the amount of heat per unit time absorbed by the punch cooling liquid in the seamless can continuous production defined by equation (3). Qd is absorbed by the die cooling liquid in the seamless can continuous production defined by equation (4). The amount of heat per unit time Qc is the amount of heat received per unit time by the can body during seamless can continuous production defined by equation (5) (3) Qp = (Tp2−Tp1) × cp × sp × Vp [J / Min]
However, in Formula (3),
cp: density of punch cooling liquid [g / cm ³ ], sp: specific heat of punch cooling liquid [J / (g · K)]
Tp1 [° C.]: Liquid temperature when the punch cooling liquid flows into the punch Tp2 [° C.] Liquid temperature when the punch cooling liquid flows out of the punch Vp: Flow rate of the punch cooling liquid [cm ³ / min]
Formula (4) Qd = (Td2-Td1) * cd * sd * Vd [J / min]
However, in Formula (4),
cd: Density of cooling liquid [g / cm ³ ], sd: Specific heat of dice cooling liquid [J / (g · K)]
Td1 [° C.]: Liquid temperature when flowing into the die Td2 [° C.]: Liquid temperature when flowing out from the die Vd: Flow rate of the die cooling liquid [cm ³ / min]
Formula (5) Qc = (Tc2-Tc1) * cc * sc * Nc [J / min]
However, in Formula (5),
cc: Mass of can barrel side wall [g], sc: Specific heat of can material [J / (g · K)]
Tc1 [° C]: Room temperature Tc2 [° C]: Can barrel side wall temperature during ironing Nc: Number of cans produced per unit time [can / min] A cup body made of a resin-coated metal plate coated with resin on at least the outer surface of the can and coated with a lubricant on both sides is dried by a punch and a die through which a coolant flows. In a resin-coated metal seamless can manufacturing apparatus for manufacturing a resin-coated metal seamless can by ironing or drawing ironing in a state,
The amount of heat absorbed per unit time absorbed by the coolant flowing through the punch during continuous production and the amount of heat absorbed per unit time absorbed by the coolant flowing through the die during continuous production. A punch endothermic coefficient calculating means for calculating a ratio of the punch endothermic amount to the total amount of each calorific value calculated from a die endothermic amount that is a heat amount and a heat amount that the can receives per unit time during continuous production, and the punch Control the flow rate of the cooling fluid of the punch and the flow rate of the cooling fluid of the die so that the endothermic wall temperature Tc2 at the time of ironing molding is not more than 80 ° C., which is the glass transition point of the resin. An apparatus for producing a resin-coated metal seamless can characterized by comprising a flow rate control means.

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