Acidic tinplating process and process for producing an iron-tin alloy on the surface of a steel sheet

Claim 2

A process for producing a steel sheet having 0.05-0.60 g/m 2 of metallic tin on said steel sheet which comprises electro-tinplating a steel sheet with an aqueous electrolyte consisting essentially of 5-150 g/l of at least one sulfate selected from the group of sulfates of alkaline metals, ammonium, aluminum, manganese or chromium in a stannous sulfate electrolyte or stannous phenolsulfonate electrolyte consisting of 1.5-50 g/l of stannous ions, 1.0-30 g/l of sulfuric acid or 3.6-106.5 g/l of phenolsulfonic acid, and 1-3 g/l of ethoxylated α-naphthol sulfonic acid and wherein the ratio of said stannous ions to said sulfuric acid or said phenolsulfonic acid is 1-3:1 or 1-3:3.6, respectively.

Claim 3

A process for producing a steel sheet having an iron-tin alloy on the surface thereof in which 0.05-1.0 g/m 2 of tin calculated from said iron-tin alloy is present on said steel sheet which comprises electro-tinplating a steel sheet with an aqueous electrolyte consisting essentially of 5-150 g/l of at least one sulfate selected from the group of sulfates of alkaline metals, ammonium, aluminum, manganese and chromium in a stannous sulfate electrolyte or stannous phenolsulfonate electrolyte consisting of 1.5-50 g/l of stannous ions, 1.0-30 g/l of sulfuric acid or 3.6-106.5 g/l of phenolsulfonic acid, and 1-3 g/l of ethoxylated α-naphthol sulfonic acid and wherein the ratio of said stannous ions to said sulfuric acid or said phenolsulfonic acid is 1-3:1 or 1-3:3.6, respectively, and heating said tin-plated steel sheet at a temperature of 232°-400° C. for 0.5-10 seconds.

Claim 4

A process for producing a steel sheet having an iron-tin alloy on the surface thereof in which 0.05-1.0 g/m 2 of tin calculated from said iron-tin alloy is present on said steel sheet which comprises electro-tinplating a steel sheet with an aqueous electrolyte consisting essentially of 5-150 g/l of at least one sulfate selected from the group of sulfates of alkaline metals, ammonium, aluminum, manganese and chromium in a stannous sulfate electrolyte or stannous phenolsulfonate electrolyte consisting of 1.5-50 g/l of stannous ions, 1.0-30 g/l of sulfuric acid or 3.6-106.5 g/l of phenolsulfonic acid, and 1-3 g/l of ethoxylated α-naphthol sulfonic acid and wherein the ratio of said stannous ions to said sulfuric acid or said phenolsulfonic acid is 1-3:1 or 1-3:3.6, respectively, and heating said tin-plated steel sheet at a temperature of 232°-400° C. for 0.5-10 seconds.

Claim 5

In a process for producing an electrotinplate in which excellent corrosion resistance is required which comprises preplating a steel sheet with tin followed by a conventional tinplating step, the improvement which comprises preplating a steel sheet by using an aqueous electrolyte containing 5-150 g/l of at least one sulfate selected from the group of sulfates of alkaline metals, ammonium, aluminum, manganese or chromium in a stannous sulfate electrolyte or stannous phenolsulfonate electrolyte consisting essentially of 1.5-50 g/l of stannous ions, 1.0-30 g/l of sulfuric acid or 3.6-106.5 g/l of phenolsulfonic acid, and 1-3 g/l of ethoxylated α-naphthol sulfonic acid and wherein the weight ratio of said stannous ions to said sulfuric acid or said phenolsulfonic acid is 1-3:1 or 1-3:3.6 at a temperature of 25° to 60° C. and under a cathodic current density of 5-50 A/dm 2 followed by tinplating the preplated steel sheet in a conventional tinplating step which is performed in an aqueous electrolyte consisting of 15-50 g/l of stannous ions, 10-30 g/l of sulfuric acid or 36-106.5 g/l of phenolsulfonic acid and 3-10 g/l of ethoxylated α-naphthol sulfonic acid at a temperature of 25° to 60° C. and under a cathodic current density of 5-50 A/dm 2 .

Claim 6

In a process for producing an electrotinplate in which excellent corrosion resistance is required which comprises preplating a steel sheet with tin followed by a conventional tinplating step, the improvement which comprises preplating a steel sheet by using an aqueous electrolyte containing 5-150 g/l of at least one sulfate selected from the group of sulfates of alkaline metals, ammonium, aluminum, manganese or chromium in a stannous sulfate electrolyte or stannous phenolsulfonate electrolyte consisting essentially of 1.5-50 g/l of stannous ions, 1.0-30 g/l of sulfuric acid or 3.6-106.5 g/l of phenolsulfonic acid, and 1-3 g/l of ethoxylated α-naphthol sulfonic acid and wherein the weight ratio of said stannous ions to said sulfuric acid or said phenolsulfonic acid is 1-3:1 or 1-3:3.6 at a temperature of 25° to 60° C. and under a cathodic current density of 5-50 A/dm 2 followed by tinplating the preplated steel sheet in a conventional tinplating step which is performed in an aqueous electrolyte consisting of 15-50 g/l of stannous ions, 10-30 g/l of sulfuric acid or 36-106.5 g/l of phenolsulfonic acid and 3-10 g/l of ethoxylated α-naphthol sulfonic acid at a temperature of 25° to 60° C. and under a cathodic current density of 5-50 A/dm 2 .