Process for the protection of galvanized steel rolled sections with a two layer chromium-chromate coating

Claim 2

A process for the protection of flat steel rolled sheets previously plated with zinc or zinc containing alloys comprising: depositing on the surface of the previous plating a layer of chromium metal having a thickness of at least about 0.55 g./m. 2 by electrodeposition; and then depositing on the surface of the layer of chromium metal a layer of chromium oxide by electrodeposition, wherein the chromium oxide layer has a thickness of at least about 0.035 g./m. 2 and the weight ratio of the chromium metal to the chromium contained in the chromium oxide in the respective deposits is from 25:1 to 4:1.

Claim 3

The process according to claim 1 in which the thickness of said chromium metal layer is about 0.55 to 1.85 g./m. 2 and the thickness of the chromium oxide layer is about 0.035 to 0.085 g./m. 2 .

Claim 4

The process according to claim 1, in which the electrodepositions of chromium metal and of chromium oxide are carried out in two stages comprising: (a) in the first stage, cathodically treating said flat rolled steel sheet previously plated with zinc or with zinc alloy in an electrolytic bath comprised of an aqueous solution of chromium anhydride and sulfate ion, wherein the chromium g./l. concentration is about 100 to 145 g./l., the weight ratio of chromium anhydride to sulfate ion g./1., from 50:1 to 150:1, the current density is from 15 to 150 A/dm. 2 and the electrolytic bath temperature is from 30° to 80°C.; and (b) in the second stage, cathodically treating the flat rolled steel section previously plated with chromium metal in an electrolytic bath comprised of an aqueous chromium anhydride solution having a chromium anhydride concentration of from 35 g./1. to 45 g./l., a pH greater than 2, a current density of from 10 to 18 A/dm. 2 and an electrolytic bath temperature of from 20° to 25° C.

Claim 5

The process according to claim 3 in which the current efficiency of the first stage electrolytic bath is increased by adding a catalyst thereto to increase the conductivity of said electrolytic bath and in which the catalyst is selected from an acid or salt bearing an ion selected from at least one member of the group consisting of F - , SiF 6 -- , BO 3 -3 , and BF 4 - .

Claim 6

The process according to claim 4 in which the acid or salt bearing an ion selected from the group consisting of F - , SiF 6 -- and BO 3 -3 is added in a concentration of from 1.2 to 1.7 g./1. and an acid or salt bearing BF 4 - is added in a per liter or concentration of from 0.4 to 0.6 ml. of a 40% solution.

Claim 7

The process according to claim 3 in which each electrodepositing stage is carried out by means of a cathode comprised of said flat steel rolled sheet and an anode selected from a member of the group consisting of lead, lead alloy, graphite, mild steel, titanium and alloys thereof, and in which the geometric position of the anode for each stage is at an angle in respect of the flat rolled section feed position of up to 90°, and said anode is in a horizontal, vertical or radial arrangement.

Claim 8

The process according to claim 3 in which in the first stage cathodic treatment the chromium anhydride concentration of the electrolytic bath is 100 to 130 g./l., the weight ratio of chromium anhydride to sulfuric acid is 90:1 to 110:1, the current density is 50 to 75 A/dm. 2 and the temperature is 45° to 65° C., and in which in the second stage cathodic treatment, the pH of the solution is 3 to 5.

Claim 9

A product obtained by means of the process according to claim 1 in which the flat rolled sheet section is in the form of a roll, plate, or sheet up to 2500 mm. wide and up to 10 μm. thick, having at least one of its sides previously plated with a zinc or zinc alloy plating of a thickness of from 1 μm to 100 μm, and in which successive electrolytic treatments have been carried out on at least one previously plated side.