Electrolytic iron metallizing of zinc surfaces

Patent metadata

Field	Value
Publication number	US-9309602-B2
Application number	US-201313795528-A
Country	US
Kind code	B2
Filing date	Mar 12, 2013
Priority date	Jun 29, 2011
Publication date	Apr 12, 2016
Grant date	Apr 12, 2016

Abstract

The present invention relates to a method for the metallizing pretreatment of galvanized and/or alloy-galvanized steel surfaces or joined metallic components having at least some zinc surfaces, wherein a thin surface layer of iron is deposited on the zinc surfaces from an aqueous electrolyte containing water-soluble compounds that are a source of iron cations. The method is performed at least partially or continuously under application of an electrolytic voltage, the galvanized and/or alloy-galvanized steel surfaces being connected as cathode. The aqueous electrolyte additionally contains an accelerator selected from oxo acids of the elements phosphorus, nitrogen and/or sulfur, the elements phosphorus, nitrogen and/or sulfur being present in moderate oxidation states.

First claim

What is claimed is:

1. A method for metallizing pretreating galvanized or alloy-galvanized steel surfaces, comprising:
contacting a galvanized or alloy-galvanized steel surface with an aqueous electrolyte, whose pH value is not greater than 9, wherein the aqueous electrolyte contains:
(a) at least one water-soluble compound which is a source of cations of the element iron, wherein the total concentration of the at least one water-soluble compound is at least 0.001 mol/l relative to the element iron,
(b) at least one accelerator selected from oxoacids of phosphorus, oxoacids of nitrogen, oxoacids of sulfur, salts of oxoacids of phosphorus, salts of oxoacids of nitrogen, salts of oxoacids of sulfur, and combinations thereof, wherein at least one of phosphorus, nitrogen, or sulfur atom of the oxoacids is present in an intermediate oxidation state, and
(c) a total of less than 10 ppm of electro-positive metal cations selected from cations of elements Ni, Co, Cu, and Sn,

wherein during a time of contact with the aqueous electrolyte, the galvanized or alloy-galvanized steel surface is switched for a period of the time of contact, at least temporarily to a cathode, wherein in this period, a cathodic electrolysis current in a range of 0.001 to 500 mA/cm 2 is imparted to the galvanized or alloy-galvanized steel surface.

2. The method according to claim 1 , wherein the at least one water-soluble compound which is a source of iron cations is present in the electrolyte in a total concentration of at least 0.01 mol/l relative to the element iron but does not exceed a total concentration in the electrolyte of 0.4 mol/l, relative to the element iron.

3. The method according to claim 1 wherein at least 50% of the iron cations are iron(II) cations.

4. The method according to claim 1 wherein the pH of the electrolyte is not less than 2 and not greater than 6.

5. The method according to claim 1 wherein the aqueous electrolyte additionally contains at least one chelating complexing agent with oxygen and/or nitrogen ligands.

6. The method according to claim 5 , wherein the chelating complexing agents are selected from triethanolamine, diethanolamine, monoethanolamine, monoisopropanolamine, aminoethylethanolamine, 1-amino-2,3,4,5,6-pentahydroxyhexane, N-(hydroxyethyl)ethylenediamine triacetic acid, ethylenediamine tetraacetic acid, diethylenetriamine pentaacetic acid, 1,2-diaminopropane tetraacetic acid, 1,3-diaminopropane tetraacetic acid, ascorbic acid, tartaric acid, lactic acid, mucic acid, gluconic acid, glucoheptonic acid, sorbital, glucose, glucamine; stereoisomers thereof; and salts thereof.

7. The method according to claim 5 , wherein a molar ratio of the chelating complexing agents to the iron cations is not greater than 5:1, but is at least 1:5.

8. The method according claim 1 , wherein the aqueous electrolyte contains no more than 2000 ppm of zinc ions.

9. The method according to claim 1 , wherein after contacting the galvanized or alloy-galvanized steel surface with the aqueous electrolyte, a metallic coating is present on the galvanized or alloy-galvanized steel surface in a coating thickness of at least 1 mg/m 2 relative to the element iron but no more than 100 mg/m 2 relative to the element iron.

10. The method according to claim 9 , wherein after contacting the galvanized or alloy-galvanized steel surface with the aqueous electrolyte thereby forming a metallizing pretreated galvanized or alloy-galvanized steel surface, a passivating conversion treatment of the metallizing pretreated galvanized or alloy-galvanized steel surface takes place, with or without an intermediate rinsing and/or drying step.

11. The method according to claim 10 , further comprising additional subsequent process steps for application of additional coatings selected from conversion coatings, organic paints, paint systems and combinations thereof.

12. The method of claim 10 , wherein the passivating conversion treatment is a chromium-free conversion treatment.

13. The method of claim 1 , wherein cations of the element iron are present in the aqueous electrolyte at a concentration of 0.01 mol/l to 0.1 mol/l.

14. The method of claim 1 , wherein the oxoacids are selected from the group consisting of hyponitrous acid, hyponitric acid, nitrous acid, hypophosphoric acid, hypodiphosphonic acid, diphosphoric (III, IV) acid, phosphonic acid, diphosphinic acid, salts thereof, and mixtures thereof.

Assignees

• Henkel Ag & Co Kgaa

Inventors

• Wolpers Michael
• Roth Marcel
• Stodt Jürgen
• Arnold Andreas

Classifications

• C25D3/20 Primary

  of iron · CPC title

• C23C22/78

  Pretreatment of the material to be coated · CPC title

• C25D5/36 Primary

  of iron or steel · CPC title