EP0260374A2 - Verfahren zur Herstellung eines mehrfach beschichteten Stahlbandes mit ausgezeichneter Korrosionsbeständigkeit und Schweissbarkeit sowie verwendbar für Container - Google Patents

Verfahren zur Herstellung eines mehrfach beschichteten Stahlbandes mit ausgezeichneter Korrosionsbeständigkeit und Schweissbarkeit sowie verwendbar für Container Download PDF

Info

Publication number
EP0260374A2
EP0260374A2 EP87104231A EP87104231A EP0260374A2 EP 0260374 A2 EP0260374 A2 EP 0260374A2 EP 87104231 A EP87104231 A EP 87104231A EP 87104231 A EP87104231 A EP 87104231A EP 0260374 A2 EP0260374 A2 EP 0260374A2
Authority
EP
European Patent Office
Prior art keywords
coating layers
nickel
tin
substrate
steel strip
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP87104231A
Other languages
English (en)
French (fr)
Other versions
EP0260374B1 (de
EP0260374A3 (en
Inventor
Kazuya Ezure
Takao Saito
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Publication of EP0260374A2 publication Critical patent/EP0260374A2/de
Publication of EP0260374A3 publication Critical patent/EP0260374A3/en
Application granted granted Critical
Publication of EP0260374B1 publication Critical patent/EP0260374B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/38—Chromatising
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10—Electroplating with more than one layer of the same or of different metals
    • C25D5/12—Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or chromium
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/48—After-treatment of electroplated surfaces
    • C25D5/50—After-treatment of electroplated surfaces by heat-treatment
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/60—Electroplating characterised by the structure or texture of the layers
    • C25D5/605—Surface topography of the layers, e.g. rough, dendritic or nodular layers

Definitions

  • the present invention relates to a process for producing a multilayer-coated steel strip having an excellent corrosion resistance and weldability and useful for producing containers. More particularly, the present invention relates to a process for producing a multilayer-coated steel strip having an excellent corrosion resistance and seam weldability, and thus is useful as a steel material for forming cylindrical portions of cans by a seam welding procedure.
  • an electrolytic tin-plate steel strip (tinplate), an electrolytic chromate-treated steel strip (TFS-CT), and an electrolytic nickel-plated steel strip (TFS-NT) are usable in the production of three piece cans by soldering, bond-bonding, or seam welding.
  • tinplate was most widely used as a steel material for producing cans, but conventional tinplate is not always satisfactory in view of the price thereof. Therefore, in order to reduce the can-producing cost, attempts have been made to reduce the thickness of the tin coating layer on the steel strip, and to utilize a seam-welding method instead of the conventional soldering method for the tinplate. It has been found, however, that when the thickness of the tin coating layer in the tinplate is reduced to a level of 0.20 ⁇ m or less, the resultant tinplate exhibits a deteriorated paint corrosion resistance and a reduced seam weldability.
  • the conventional TFS-NT sometimes used as a steel material for producing seam-welded cans usually exhibits a satisfactory seam weldability, but this weldability is not always satisfactory in practical use. Also, the conventional TFS-NT has a satisfactory paint corrosion resistance in usual use, but the level of the paint corrosion resistance is not always satisfactory when brought into contact with a corrosive material, for example, strongly acidic food.
  • Japanese Unexamined Patent Publication (Kokai) No. 60-75586 discloses a process for producing a coated steel strip.
  • a steel strip is coated with a small amount of nickel, and the nickel-coated steel strip is then plated with tin.
  • the nickel and tin coated-steel strip is heat treated, and the tin coating layer is converted to an Fe-Sn alloy layer, the presence of the small amount of nickel coating layer causes the structure of the Fe-Sn alloy layer to exhibit an enhanced density. Therefore, the resultant coated steel strip exhibits an improved corrosion resistance.
  • the presence of the nickel coating layer is effective for restricting the Fe-Sn alloy-forming reaction in the heat-treatment, and thus the resultant coated steel exhibits an enhanced seam weldability.
  • the inventors of the present invention have found that the properties, for example, seam weldability and corrosion resistance, of the coated steel strip usable as a steel material for seam welded cans, vary depending on the distribution of metallic tin coating over the surface of a steel strip substrate. That is, it has been found that the properties of the coated steel strip over which the metallic tin layer is unevenly distributed and having an uneven rough surface, are better than those of a coated steel strip over which the metallic tin layer is evenly distributed and having a smooth uniform surface.
  • the coated steel strip having an uneven thin tin coating layer exhibits a better seam weldability and corrosion resistance than those of a conventional coated steel strip having an even thin tin coating layer.
  • Fujimoto et al, "Iron and Steel", vol. 72, No. 5, page 39. 1986 discloses that, in order to provide a tin coating layer having an uneven thickness with a stable reproductivity, it is effective to apply an anodic electrolytic treatment to the steel strip in an alkaline treating liquid before the nickel-plating step.
  • the resultant coated steel strip is unsatisfactory from the viewpoint of corrosion resistance and weldability.
  • An object of the present invention is to provide a process for producing a multilayer-coated steel strip having an excellent corrosion resistance and weldability and useful for producing cans or containers with an improved reproductivity.
  • the above-mentioned object can be attained by the process of the present invention which comprises the steps of (A) plating a substrate consisting of a steel strip with metallic nickel or a nickel-based alloy to form, on both the upper and lower surfaces of the substrate, nickel-based coating layer, each of which layers is coated in an average amount of 2 to 100 mg/m 2 and is provided with a number of convex and concave portions, and in which layer portions thereof having a coating thickness of 0.001 ⁇ m or more have a total area corresponding to 10% to 95% of the entire area of the surfaces of the substrate; (B) coating the nickel-based plated substrate with tin to form tin coating layers on the nickel-based coating layers, each of which tin coating layers is coated in an average amount of 200 to 2000 mg/m 2 , to provide a precursory coated steel strip; (C) heating the precursory coated steel strip at a temperature equal to or higher than the melting point of the tin coating layer, to cause the nickel-based coating layers and the tin
  • a substrate consisting of a steel strip to be multilayer-coated is plated with nickel or a nickel-based alloy to form nickel-based coating layers on both the upper and lower surfaces of the substrate to an extent such that the resultant nickel-based coating layers are coated in a small average amount of from 2 to 100 mg/m , preferably from 5 to 100 mg/m , per surface of the substrate and have an uneven thickness distribution, so as to provide a number of convex and concave portions preferably substantially evenly distributed in the layer.
  • the uneven nickel based coating layer may be, as shown in Fig. 2, in the form of a land having a number of mountains and hills corresponding to the convex portions and a number of lakes and valleys corresponding to the concave portions, which mountains, hills, lakes, and valleys are substantially evenly distributed in the land.
  • Some of the lakes and valleys (concave portions) may have bottoms thereof formed by nickel or a nickel-based alloy plated on the substrate surfaces. Also, in the bottoms of other lakes and valleys (concave portions), portions of the substrate surfaces may be exposed to the outside. That is, the nickel-based coating layer may incompletely cover the surfaces of the substrate.
  • the uneven nickel-based coating layer may be, as shown in Fig. 2, in the form of a number of islands corresponding to the convex portions, consisting of nickel or the nickel-based alloy and preferably substantially evenly distributed in one or more seas corresponding to the concave portions connected to each other.
  • Some of the island portions may be in the above-mentioned form of a land having a number of mountains, hills, lakes, and valleys. In the bottoms of the sea portions of the nickel-based coating layer, the corresponding portions of the substrate surfaces are exposed to the outside.
  • a surface of a steel strip substrate 1 is coated with an uneven nickel-based coating layer 2 having convex portions 2a and concave portions 2b.
  • a surface of a steel strip substrate 1 is coated with an islands-in-sea type nickel-based coating layer 2 consisting of a plurality of island- formed nickel-based coating deposits 2c separated from each other. Portions la of the surface of the substrate 1 are exposed to the outside but not coated with the nickel-based coating deposit.
  • the coating thicknesses of the convex portions may be different.
  • the coating thicknesses of the concave portions that is, the thickness between the surface of the substrate and the bottoms of the concave portions, may be different.
  • the total area of portions of the layers having a coating thickness of 0.001 um or more must be coated to a level corresponding to 10% to 95%, preferably, 10% to 90%, of the entire area of the surfaces of the substrate to be coated.
  • the convex and concave portions of the resultant nickel-based coating layers satisfy the relationships (1), (2), and (3):
  • the steel strip substrate which has been degreased or surface cleaned by an ordinary method, is subjected to a nickel-plating process.
  • the steel strip substrate may be subjected to an anodic electrolytic treatment in a pickling liquid, for example, a sulfuric acid aqueous solution, or a degreasing liquid, for example, a sodium hydroxide aqueous solution.
  • the surface cleaned steel strip substrate is unevenly plated with nickel or a nickel-based alloy in an amount of 2 to 100 mg/m , preferably 5 to 100 mg/m , per surface of the substrate.
  • the plating process can be carried out in an ordinary nickel plating liquid, for example, a sulfuric acid watt plating liquid.
  • the composition of the plating liquid, plating current density, plating temperature and time, and other plating conditions are determined so that the resultant nickel-based coating layers are in the above-mentioned specific amount and have the above-mentioned uneven thickness distribution.
  • the plating method is not limited to a specific method and may be an electric plating method or a non-electrolytic plating method, as long as the specific uneven nickel-based coating layers is obtained.
  • the nickel-based plated substrate may be additionally subjected to an anodic electrolytic treatment.
  • the nickel-based plated substrate may be subjected to a heat treatment at an elevated temperature, to cause the plated nickel or nickel-based alloy to diffuse into the steel strip substrate.
  • the resultant coating layer will have a substantially even thickness and it will be difficult to provide a coated steel strip having a satisfactory corrosion resistance and weldability.
  • the amount of the plated nickel or nickel-based alloy is less than 2 mg/m 2 , it will be difficult to provide a dense Fe-Ni-Sn based base layer having a excellent effect for enhancing the corrosion resistance of the resultant coated steel strip.
  • the limitation in the amount of the nickel-based coating layers to the range of from 2 to 100 mg/m 2 per surface of the substrate is very important when causing the resultant nickel-based coating layers to have an uneven coating thickness distribution and to be provided with a number of convex portions and concave portions thereof.
  • This specific form of the nickel based coating layers is essential when providing a multilayer-coated steel strip having an excellent corrosion resistance and weldability and useful as a steel material for producing cans or containers.
  • the total area of the portions of the nickel-based coating layers having a thickness of 0.001 ⁇ m or more is more than 95% or less than 10% of the entire area of the surfaces of the substrate, the unevenness in the coating thickness of the nickel-based coating layers will be unsatisfactory, and thus the resultant coated steel strip will exhibit an unsatisfactory corrosion resistance and weldability.
  • the uneven nickel-based coating layer satisfying the above-defined relationships (1), (2), and (3) is very effective for further enhancing the corrosion resistance and weldability of the resultant coated steel strip.
  • the uneven distribution of the thickness of the nickel-based coating layer can be observed by means of an electron probe micro-analyser or an Auger electron Spectroscopy.
  • the uneven nickel-based coating layer may consist of nickel or a nickel-based alloy consisting of at least 80% by weight of nickel and 20% by weight or less of an additional metal element consisting of at least one member selected from zinc, phosphorus, cobalt, copper, and chromium.
  • the additional metal element can be alloyed with nickel by the heating treatment and is effective for causing a portion of tin coating layer to remain in the free tin state after the heat treatment. The remaining free tin forms an intermediate tin coating layer on the base coating layer after the heat-treatment step.
  • the nickel-based plated substrate is coated with tin in an average amount of 200 to 2000 mg/m 2 per surface of the substrate to provide a precursory coated steel strip.
  • the tin coating procedures are not limited to a specific method, and can be carried out by any conventional tin plating method. However, the tin coating is preferably carried out by an electric plating method.
  • the average amount of the tin coating layers formed on the nickel based plated substrate is limited to a specific range from 200 to 2000 mg/m 2 per surface of the substrate to provide a resultant coated steel strip having an excellent corrosion resistance and weldability at a low cost.
  • the average amount of the tin coating layers is more than 2000 mg/m 2 , the excess amount of tin over 2000 mg/m 2 has no effect on the enhancing of the corrosion resistance and weldability of the resultant coated steel strip, and undesirably increased the cost of the resultant coated steel strip. Also, an average amount of less than 200 mg/m 2 of the tin coating layer results in an unsatisfactory seam weldability and corrosion resistance of the resultant coated steel strip.
  • the coated steel strip is usually washed with water and, if necessary, is immersed in a flux comprising, as a principal component, phenol sulfonic acid or ammonium chloride, and finally, is dried.
  • the flux may have a concentration corresponding to from 1/2 to 1/3 of that in an ordinary flux for producing a usual tinplate.
  • the necessity for flux treatment and composition and concentration of the flux can be decided in consideration of the type and constitution of the desired coated steel strip.
  • the precursory coated steel strip is heat-treated at a temperature equal to or higher than the melting point of the tin coating layer.
  • This heat treatment may be carried out by, for example, an electric resistance-heating method or high-frequency induction heating method. Further, this heat treatment may be effected in an atmosphere consisting of an inert gas, for example, nitrogen or argon gas.
  • the heat treatment applied to the precursory coated steel strip is effective for converting the nickel-based coating layers and tin coating layers to base coating layers formed on the two surfaces of the substrate, and consisting essentially of an Fe-Ni-Sn-based alloy and having a number of convex and concave portions, and intermediate coating layers formed on the base coating layers, consisting essentially of tin and having a number of convex and concave portions.
  • the heat treatment is controlled to an extent such that the content of tin in the resultant base Fe-Ni-Sn-based alloy coating layers corresponds to about 1/3, that is, from 30% to 35% of the entire weight of the original tin-coating layers.
  • the heat treatment at a temperature equal to or higher than the melting point of the original tin coating layer results in the conversion of the nickel-based coating layers and the tin coating layers to base Fe-Ni-Sn-based alloy coating layers and intermediate tin coating layers, which are effective for imparting an excellent corrosion resistance and weldability to the resultant coated steel strip.
  • a precursory coated steel strip 10 which has been produced by the first and second steps of the process of the present invention, has a steel strip substrate 11, an islands-in-sea type nickel-based coating layer 12 having a number of islands 12a, wherein the islands 12a are separated from each other, and sea-shaped portions 12b between the islands 12a, and a tin coating layer 13.
  • the precursory coated steel strip is heated at a temperature equal to or higher than the melting point of the tin coating layer, the tin coating layer 13 is melted and the nickel-based coating layer 12 is alloyed with a portion of iron in the steel strip substrate 11 and a portion of tin in the tin coating layer 13.
  • the alloying rate of nickel or nickel based alloy with the iron and tin is proportional to the concentration of nickel or nickel-based alloy in the alloying system. Therefore, each of the nickel-based islands 12a are rapidly converted to a corresponding alloy coating while growing three-dimensionally. Namely, each alloy coating becomes thicker than the corresponding nickel-based islands and spreads on the substrate surface.
  • the spread alloy coatings are connected to each other and form a continuous alloy coating layer which substantially completely covers the surface of the substrate, as shown in Fig. 3B.
  • the resultant alloy coating layer 14 has a number of convex portions 14a corresponding to the nickel-based islands 12a and a number of concave portions 14b corresponding to the sea-shaped portion 12b in the nickel-based coating layer 12 in Fig. 3A.
  • the tin melt exhibits a larger wetting affinity and a smaller free interface energy to the Fe-Ni-Sn-based alloy layer surface than to the nickel based alloy layer surface and to the steel strip surface.
  • the larger the thickness of the Fe-Ni-Sn-based alloy layer the greater the wetting affinity of the tin melt thereto. Accordingly, the thickness of the tin melt layer 15 on the Fe-Ni-Sn-based alloy layer 14 corresponds to the thickness of the Fe-Ni-Sn-based alloy layer 14 as shown in Fig.
  • the resultant tin coating layer 15 has a number of convex portions 15a and concave portions 15b thereof respectively corresponding to the convex portions 14a and the concave portions 14b of the alloy coating layer 14.
  • the even base alloy coating layer causes the intermediate tin coating layer to have a substantially even thickness.
  • the even tin coating layer sometimes can be converted to an uneven tin coating layer as shown in Fig. 3B by a flux treatment under a certain condition.
  • the conversion by the flux treatment is not always successful.
  • the flux treatment fails to convert the even tin coating layer to an uneven tin coating layer.
  • the flux treated tin coating layer contains uneven portions and even portions thereof. In other words, the flux treatment cannot stably convert the even tin coating layer to an uneven tin coating layer and, therefore, is not valuable for stably producing the coated steel strip having an enhanced corrosion resistance and weldability.
  • the uneven tin coating layers can be stably produced by utilizing the uneven nickel-based coating layers formed on the steel strip substrate surfaces.
  • the uneven tin coating layers are very effective for producing the coated steel strip having an enhanced weldability and corrosion resistance, and therefore, useful for cans and containers.
  • the convex portions are spaced 1 to 30 pm apart, and have a coating thickness of 0.20 um or more, the concave portions have a coating thickness of 0 to 0.07 ⁇ m, and the average coating thickness of the entire intermediate tin coating layers is 0.17 ⁇ m or less.
  • an electrolytic chromate treatment is applied, as a final passive state-forming step, to the heat-treated steel strip to form electrolysed chromate surface coating layers on the intermediate tin coating layers.
  • the resultant surface coating layers have substantially plain surfaces. That is, the thicknesses of portions of the surface coating layers formed on the convex portions of the intermediate tin coating layers is larger than that of portions of the surface coating layer formed on the concave portions of the intermediate tin coating layer.
  • the surface coating layer 16 has a number of downward convex portions 16a formed on the concave portions 15b of the intermediate tin coating layer 15 and a number of upward concave portions 16b formed on the convex portions 15a of the intermediate tin coating layer 15.
  • the upward concave portions 16b of the surface coating layers having a small coating thickness exhibit an excellent weldability.
  • the downward convex portions 16a of the surface coating layers having a large coating thickness exhibit a superior corrosion resistance. Therefore, as a whole, the coated steel strip of the present invention exhibits an enhanced weldability and corrosion resistance and is useful for cans and containers.
  • the concave portions of the uneven surface coating layers having a small coating thickness serve to stabilize the flow of the electric current, and thus to improve the seam weldability of the coated steel strip.
  • the thick convex portions of the surface coating layers are effective for enhancing the corrosion resistance of the coated steel strip.
  • the uneven surface coating layers consisting essentially of electrolysed chromate can be produced by a conventional electrolytic chromate-treating method usable for TFS-CT.
  • the electrolytic chromate treatment is carried out in accordance with a cathodic reduction method in an aqueous solution of chromic anhydride in the presence or absence of anions, for example, sulfuric anions or fluoride anions.
  • any known means for reducing co-depositing anions in the electrolysed chromate layer can be applied to the electrolytic chromate treatment.
  • the electrolysed chromate surface coating layer may consist essentially of chromium oxide hydrate alone.
  • the surface coating layer is preferably in an average amount, in terms of metallic chromium, of 3 to 30 mg/m 2 per surface of the substrate. If the average amount is less than 3 mg/m 2 , the resultant coating steel strip sometimes exhibits an unsatisfactory corrosion resistance and a poor bonding property to paint. Also, if the average amount of the surface coating layers is more than 30 mg/m 2 , the resultant coating steel strip sometimes exhibits an unsatisfactory weldability.
  • the electrolysed chromate surface coating layer may comprise hot alkali-soluble chromium fractions and hot alkali-insoluble chromium fractions.
  • the proportion in weight of the hot alkali-soluble fractions to the hot alkali-insoluble fractions is not limited to a specific level. However, in the concave portions of the surface coating layers, preferably the proportion of the hot alkali-insoluble fractions is larger than that of the hot alkali-insoluble fractions.
  • a specimen that is, a piece of a multilayer coated steel strip, was formed into a peripheral portion of a can in which edge portions of the specimen were overlapped to a width of 0.4 mm.
  • the overlapped portion of the specimen was seam welded under a pressure of 45 hgf at a can-forming rate of 45 mpm.
  • the value of the second order welding current was varied to determine a range of values of the second order welding current, in which range an optimum seam welding was obtained.
  • the lower limit of the optimum range of the second order welding current corresponded to a second order welding current value at which the resultant welded portion exhibited a lowest value of satisfactory welding strength.
  • the upper limit of the optimum second order welding current value range corresponded to an upper limit of the second order welding current value range in which the seam welding procedure can be carried out without the generation of an undesirable splash phenomenon.
  • the welding strength of the welded portion was determined by an impact test and a peeling test in which a V-shaped notch was formed in the welded portion of the specimen and the welded two ends of the specimen were peeled from each other by a pair of pincers.
  • the appearance of the seam welded portion of the specimen was evaluated by naked eye observation in which the generation and intensity of expulsion and surface flash on the welded portion were observed.
  • the specimen to be subjected to the seam welding test was preliminarily heated at a temperature of 210°C for 20 minutes in an electric air oven.
  • Two surfaces of a specimen were coated with an ordinary epoxy-phenol coating material for cans, in an amount of 55 mg/dm 2 per surface of the specimen, by a roll coating method and the resultant coating layers were heated at a temperature of 205°C for 10 minutes and then further heated at a temperature of 190°C for 10 minutes.
  • the resultant paint layers were scratched with a cutting knife and then subjected to an Ericksen process at a height of 5 mm by using an Ericksen testing machine.
  • the resultant testing specimen was subjected to a salt water spraying test for one hour, by spraying an aqueous solution of 5% by weight of NaCl. Then the specimen was left in a thermo-hydrostat at a temperature of 25°C at a relative humidity of 85% for 14 days. The generation of rust in the scratched portions in the specimen was observed by the naked eye.
  • the resultant nickel coating layers were in the form as indicated in Table 1 and had the largest coating thickness (hmax) and the percentage RA of the total area portions of the nickel coating layers having a coating thickness f 0.001 ⁇ m or more based on the entire area of the surfaces of the substrate, as shown in Table 1.
  • the form and thickness of the nickel coating layers were determined by AES and EPMA analyses.
  • the largest thickness (hmax) of the nickel coating layers was 0.002 ⁇ m or more and the percentage RA of the portions of the nickel coating layers having a coating thickness of 0.001 ⁇ m or more was in the range of from 10% to 95%.
  • the nickel-coated steel strip was plated with tin in a tin plating aqueous liquid containing 25 g/1 of tin sulfate, 30 g/l of phenol sulfonic acid, and 2 g/1 of ethoxylated a-naphthol sulfonic acid at a temperature in the range of from 40 to 50°C at a cathodic current density of 20 A/dm 2 .
  • the average amount of the resultant tin coating layers was in the range of from 800 to 1000 mg/m 2 per surface of the substrate, as shown in Table 1.
  • the resultant precursory coated steel strip was immersed in an aqueous flux solution containing 1 to 2 g/1 of phenol sulfonic acid at a temperature of 45°C, and then dried.
  • the flux-treated precursory coated steel strip was heat-treated by an electric resistance heating method at a temperature of from 240°C to 280°C for 2 seconds to 6 seconds in the air atmosphere.
  • the heating temperature and time were decided so that the resultant Fe-Ni-Sn alloy base layer contained tin in an amount corresponding to about 1/3 of the entire amount of tin plated on the substrate.
  • the heat-treated steel strip was subjected to an electrolytic chromate treatment in an aqueous treating solution containing 2 to 100 g/1 of Cr0 3 , 0.1 to 1.0 g/1 of H 2 S0 4 and 0 to 3 g/1 of Na 2 SiF 6 at a temperature of from 40°C to 60°C at a cathodic current density in the range of from 5 to 90 A/dm 2 so as to form electrolysed chromate surface coating layers in an average amount of 12 to 17 mg/m 2 , in terms of metallic chromium, per surface of the substrate.
  • the distribution of the electrolysed chromate in the surface coating layers was determined from the characteristic X-ray intensity of chromium measured by EPMA analysis.
  • even distribution refers to a distribution of thickness of the intermediate tin coating layers in such a manner that the ratio of the average thickness T V of the downward convex portions to the average thickness T C of the upward concave portions of the surface coating layers is 1 or more and less than 1.2.
  • uneven distribution refers to a distribution of thickness of the intermediate tin coating layers in such a manner that the ratio of the average thickness T V of the downward convex portions to the average thickness T C of the upward concave portions of the surface coating layers is 1.2 or more.
  • the surface coating layers have an uneven thickness distribution.
  • the nickel-plating step was carried out so that the resultant nickel coating layers were as indicated in Table 1.
  • the tin-coating step was carried out in an aqueous plating solution containing 75 g/1 of stannous chloride, 25 g/1 of sodium fluoride, 50 g/1 of potassium hydrogen fluoride, and 45 g/1 of sodium chloride at a temperature in the range of from 40 to 50°C and at a cathodic current density in the range of from 20 to 40 A/ dm 2 , so that the resultant tin coating layers had the average amount as indicated in Table 1.
  • Comparative Examples 4 and 5 the same procedures as those mentioned in Example 1 were carried out except that the nickel plating step was omitted, and in Comparative Example 5, the average amount of the tin coating layer was 1100 mg/m 2 per surface of the substrate.
  • An ordinary tinplate #25 having tin coating layers in an amount of 2800 mg/m 2 per surface of the tinplate was subjected to the same electrolytic chromate treatment and tests as those mentioned above.
  • Example 1, 2, 3 and 6 the resultant multilayer-coated steel strips exhibited excellent seam weldability and corrosion resistance compatible with those of the ordinary tinplate, although the amounts of the tin coating layers in Examples 1, 2, 3 and 6 are in a low level of from 800 or 1000 mg/m 2 , whereas the ordinary tinplate had a large amount of tin coating layers of 2800 mg/m .

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating Methods And Accessories (AREA)
EP87104231A 1986-09-18 1987-03-23 Verfahren zur Herstellung eines mehrfach beschichteten Stahlbandes mit ausgezeichneter Korrosionsbeständigkeit und Schweissbarkeit sowie verwendbar für Container Expired - Lifetime EP0260374B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP220521/86 1986-09-18
JP61220521A JPS6376896A (ja) 1986-09-18 1986-09-18 シ−ム溶接性、耐食性に優れた表面処理鋼板の製造方法

Publications (3)

Publication Number Publication Date
EP0260374A2 true EP0260374A2 (de) 1988-03-23
EP0260374A3 EP0260374A3 (en) 1989-09-06
EP0260374B1 EP0260374B1 (de) 1993-11-18

Family

ID=16752317

Family Applications (1)

Application Number Title Priority Date Filing Date
EP87104231A Expired - Lifetime EP0260374B1 (de) 1986-09-18 1987-03-23 Verfahren zur Herstellung eines mehrfach beschichteten Stahlbandes mit ausgezeichneter Korrosionsbeständigkeit und Schweissbarkeit sowie verwendbar für Container

Country Status (5)

Country Link
EP (1) EP0260374B1 (de)
JP (1) JPS6376896A (de)
AU (1) AU573122B2 (de)
CA (1) CA1331962C (de)
DE (1) DE3788178T2 (de)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0725453A1 (de) * 1993-10-22 1996-08-07 TOYO KOHAN Co., Ltd Oberflächenbehandeltes stahlblech für batteriegehäuse und batteriegehäuse
CN104790002A (zh) * 2015-03-13 2015-07-22 武汉钢铁(集团)公司 一种五金制品包装用双复合镀层耐磨捆带的生产方法
CN115175466A (zh) * 2022-07-04 2022-10-11 江苏富乐华半导体科技股份有限公司 一种提升陶瓷覆铜基板表面电镀锡镍合金的焊接方法

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0660434B2 (ja) * 1987-04-01 1994-08-10 日本鋼管株式会社 表面処理鋼板の製造方法
JP2580923B2 (ja) * 1991-12-27 1997-02-12 日本鋼管株式会社 溶接缶用ラミネート鋼板とその製造方法
JP4742641B2 (ja) * 2005-03-28 2011-08-10 Ｊｆｅスチール株式会社 溶接缶用錫めっき鋼板の製造方法
CN105177641A (zh) * 2015-10-27 2015-12-23 姜少群 一种镀镍钢制壳体

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2478680A1 (fr) * 1980-03-18 1981-09-25 Toyo Kohan Co Ltd Procede de production d'une feuille d'acier a revetement d'etain extremement mince et produit obtenu
FR2483470A1 (fr) * 1980-06-03 1981-12-04 Nippon Steel Corp Feuillard d'acier enduit d'oxyde de chrome hydrate, utilisable pour des bidons et d'autres reservoirs soudes
EP0055481A2 (de) * 1980-12-29 1982-07-07 Nippon Steel Corporation Mit Chrom plattiertes Stahlband mit ausgezeichneter Schweissbarkeit und Korrosionsbeständigkeit und Verfahren zu seiner Herstellung
EP0063933A1 (de) * 1981-04-23 1982-11-03 Nippon Steel Corporation Stahlblech mit unterschiedlichen Mehrschichtüberzügen, geeignet für Konservendosen
EP0164092A1 (de) * 1984-06-04 1985-12-11 Kawasaki Steel Corporation Verfahren zur Herstellung von Stahlbändern die eine Oberflächenbehandlung untergangen sind und geeignet sind für elektrisches Widerstandsschweissen
US4601957A (en) * 1984-04-13 1986-07-22 Toyo Kohan Co., Ltd. Method for producing a thin tin and nickel plated steel sheet for welded can material

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54142135A (en) * 1978-04-28 1979-11-06 Nippon Kokan Kk <Nkk> Tin-plated steel plate and its manufacture
JPS61130500A (ja) * 1984-11-29 1986-06-18 Kawasaki Steel Corp Ｓｎ／Ｃｒ２層めつき鋼板の製造方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2478680A1 (fr) * 1980-03-18 1981-09-25 Toyo Kohan Co Ltd Procede de production d'une feuille d'acier a revetement d'etain extremement mince et produit obtenu
FR2483470A1 (fr) * 1980-06-03 1981-12-04 Nippon Steel Corp Feuillard d'acier enduit d'oxyde de chrome hydrate, utilisable pour des bidons et d'autres reservoirs soudes
EP0055481A2 (de) * 1980-12-29 1982-07-07 Nippon Steel Corporation Mit Chrom plattiertes Stahlband mit ausgezeichneter Schweissbarkeit und Korrosionsbeständigkeit und Verfahren zu seiner Herstellung
EP0063933A1 (de) * 1981-04-23 1982-11-03 Nippon Steel Corporation Stahlblech mit unterschiedlichen Mehrschichtüberzügen, geeignet für Konservendosen
US4601957A (en) * 1984-04-13 1986-07-22 Toyo Kohan Co., Ltd. Method for producing a thin tin and nickel plated steel sheet for welded can material
EP0164092A1 (de) * 1984-06-04 1985-12-11 Kawasaki Steel Corporation Verfahren zur Herstellung von Stahlbändern die eine Oberflächenbehandlung untergangen sind und geeignet sind für elektrisches Widerstandsschweissen

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0725453A1 (de) * 1993-10-22 1996-08-07 TOYO KOHAN Co., Ltd Oberflächenbehandeltes stahlblech für batteriegehäuse und batteriegehäuse
EP0725453A4 (de) * 1993-10-22 1996-08-21
CN104790002A (zh) * 2015-03-13 2015-07-22 武汉钢铁(集团)公司 一种五金制品包装用双复合镀层耐磨捆带的生产方法
CN115175466A (zh) * 2022-07-04 2022-10-11 江苏富乐华半导体科技股份有限公司 一种提升陶瓷覆铜基板表面电镀锡镍合金的焊接方法
CN115175466B (zh) * 2022-07-04 2023-06-06 江苏富乐华半导体科技股份有限公司 一种提升陶瓷覆铜基板表面电镀锡镍合金的焊接方法

Also Published As

Publication number Publication date
EP0260374B1 (de) 1993-11-18
AU573122B2 (en) 1988-05-26
CA1331962C (en) 1994-09-13
JPH0214438B2 (de) 1990-04-09
AU7071287A (en) 1988-03-24
EP0260374A3 (en) 1989-09-06
DE3788178D1 (de) 1993-12-23
DE3788178T2 (de) 1994-03-10
JPS6376896A (ja) 1988-04-07

Similar Documents

Publication Publication Date Title
US4601957A (en) Method for producing a thin tin and nickel plated steel sheet for welded can material
US4501802A (en) Hydrated chromium oxide-coated steel strip useful for welded cans and other containers
US4861441A (en) Method of making a black surface treated steel sheet
CA1230954A (en) Surface-treated steel strips seam weldable into cans
US4421828A (en) Steel sheet carrying a protective layer and process for producing such a sheet
JPH0216397B2 (de)
EP0260374B1 (de) Verfahren zur Herstellung eines mehrfach beschichteten Stahlbandes mit ausgezeichneter Korrosionsbeständigkeit und Schweissbarkeit sowie verwendbar für Container
CA1187660A (en) Steel strip having differentiated multilayer coatings and being useful for manufacture of cans
CA2190817C (en) Zinciferous plated steel sheet and method for manufacturing same
EP0164092B1 (de) Verfahren zur Herstellung von Stahlbändern die eine Oberflächenbehandlung untergangen sind und geeignet sind für elektrisches Widerstandsschweissen
JPH0154437B2 (de)
JPS62103390A (ja) 製缶用薄Ｓｎメツキ鋼板及びその製造方法
JPH0472091A (ja) ２ピース缶用表面処理鋼板及びその製造方法
JPS6029477A (ja) 溶接性と塗装性能にすぐれた缶容器用鋼板の製造法
CA1179629A (en) Process for producing a chromium-plated steel strip having enhanced weldability
GB2126249A (en) Zinc and tin plated steel sheet
JPS62139898A (ja) シ−ム溶接性に優れた製缶用表面処理鋼板
KR900004071B1 (ko) 시임(seam) 용접성, 도료 밀착성이 우수한 표면처리 강판 및 그 제조방법
JP3270318B2 (ja) 溶接性、耐食性、外観性および密着性に優れた溶接缶用鋼板
JPS6396294A (ja) 溶接性、耐食性に優れた缶用鋼板の製造方法
KR890004621B1 (ko) 용접제관용 표면 처리강판 및 그의 제조방법
JPS6379994A (ja) 溶接缶用鋼板の製造方法
JPS5989784A (ja) 塗装後の耐食性にすぐれた溶接缶用鋼板の製造方法
JPS59197597A (ja) 塗装後耐食性に優れた溶接缶用ニツケルめつき鋼板の製造方法
JPH0441694A (ja) 溶接性に優れた薄錫めっき鋼板の製造方法

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): BE DE FR GB IT LU NL

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): BE DE FR GB IT LU NL

17P Request for examination filed

Effective date: 19891025

17Q First examination report despatched

Effective date: 19910723

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): BE DE FR GB IT LU NL

ITF It: translation for a ep patent filed
REF Corresponds to:

Ref document number: 3788178

Country of ref document: DE

Date of ref document: 19931223

ET Fr: translation filed
EPTA Lu: last paid annual fee
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20060305

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20060308

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20060316

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20060322

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: LU

Payment date: 20060328

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20060331

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20060509

Year of fee payment: 20

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20070322

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20070323

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20070323

BE20 Be: patent expired

Owner name: *NIPPON STEEL CORP.

Effective date: 20070323