Composition and method for treatment of phosphated metal surfaces

• US 5,662,746 A
• Filed: 02/23/1996
• Issued: 09/02/1997
• Est. Priority Date: 02/23/1996
• Status: Expired due to Fees

• Current Assignee: Brent America, Inc.
• Original Assignee: Brent America, Inc.
• Inventors: Affinito, John C.
• Primary Examiner(s): Silverberg, Sam
• Application Number:
  US08/605,959
• Time in Patent Office: 557 Days
• Field of Search: 148/257, 148/247
• US Class Current: 148/247
• CPC Class Codes: C23C 22/83 Chemical after-treatment

Abstract

A rinse solution for the treatment of conversion-coated metal substrates for improving the adhesion and corrosion resistance of siccative coatings, comprising an aqueous solution of a Group IVA metal ion, namely, zirconium, titanium, hafnium, and mixtures thereof, and a phenol polymer, with the pH of the total solution about 3.5 to 5.1. A method for treating such materials by applying the rinse solution to the substrate.

Claims

1. A rinse solution for the treatment of conversion-coated metal substrates for improving the adhesion and corrosion resistance of siccative coatings, comprising an aqueous solution of a Group IVA metal ion, selected from the group consisting of zirconium, titanium, hafnium, and mixtures thereof, and a phenolic resin in a concentration of about 0.01 to 0.40% w/w, with the Group IVA metal ion in a concentration of about 0.00035 to 0.0050% w/w, and the pH for the entire solution about 3.5 to 5.1, with the phenolic resin being a water soluble base catalyzed condensation product of the reaction between phenol and formaldehyde.

2. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w.

3. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w, with a pH of about 3.5 to 5.1.

4. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0010% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

5. A rinse solution as defined in claim 1 wherein the zirconium ion concentration in the rinse solution is about 0.00065 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w.

6. A rinse solution as defined in claim 1 wherein the zirconium ion concentration in the rinse solution is about 0.00065 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w, with a pH of about 3.5 to 5.1.

7. A rinse solution as defined in claim 1 wherein the zirconium ion concentration in the rinse solution is about 0.00065 to 0.0011% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

8. A rinse solution as defined in claim 1 wherein the hafnium ion concentration in the rinse solution is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w.

9. A rinse solution as defined in claim 1 wherein the hafnium ion concentration in the rinse solution is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w, with a pH of about 3.5 to 5.1.

10. A rinse solution as defined in claim 1 wherein the hafnium ion concentration in the rinse solution is about 0.0008 to 0.0010% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

11. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the zirconium concentration is about 0.00065 to 0.0011% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

12. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the hafnium concentration is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

13. A rinse solution as defined in claim 1 wherein the hafnium ion concentration in the rinse solution is about 0.00035 to 0.0050% w/w and the zirconium concentration is about 0.00065 to 0.0011% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

14. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the zirconium concentration is about 0.00065 to 0.0011% w/w and the hafnium ion concentration is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

15. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0010% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1, where the solution is applied by means of spraying.

16. A rinse solution as defined in claim 1 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0010% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1, where the solution is applied by means of dipping.

17. A rinse solution as defined in claim 1 wherein the Group IVA metal ion is from a Group IVA metal ion source selected from the group consisting of hexafluorozirconic acid, hexafluorotitanic acid, hafnium oxide, titanium oxysulfate, titanium tetrafluoride, zirconium sulfate and mixtures thereof.

36. A rinse solution as defined in claim 1 wherein the phenolic resin is a mixture of substituted phenol compounds, selected from the group consisting of 2-hydroxybenzyl alcohol, 4-hydroxybenzyl alcohol, 2,6-dimethylol phenol, 2,4-dimethylol phenol and 2,4,6-trimethylol phenol.

18. In a method for treating conversion-coated metal substrates for improving the adhesion and corrosion resistance of siccative coatings, wherein the improvement comprises:

providing an aqueous solution of a Group IVA metal ion, selected from the group consisting of zirconium, titanium, hafnium, and mixtures thereof, and a phenolic resin in a concentration of about 0.01 to 0.40% w/w, with the phenolic resin being a water soluble base catalyzed condensation product of the reaction between phenol and formaldehyde;

providing the Group IVA metal ion concentration at about 0.00035 to 0.0050% w/w;

providing a pH of the solution of about 3.5 to 5.1; and

applying the solution to the substrate.

19. The method as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w.

20. The method as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w, with a pH of about 3.5 to 5.1.

21. The method as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0010% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pit of about 4.0 to 5.1.

22. The method as defined in claim 18 wherein the zirconium ion concentration in the rinse solution is about 0.00065 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w.

23. The method as defined in claim 18 wherein the zirconium ion concentration in the rinse solution is about 0.00065 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w, with a pH of about 3.5 to 5.1.

24. The method as defined in claim 18 wherein the zirconium ion concentration in the rinse solution is about 0.00065 to 0.0011% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

25. The method as defined in claim 18 wherein the hafnium ion concentration in the rinse solution is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w.

26. The method as defined in claim 18 wherein the hafnium ion concentration in the rinse solution is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.40% w/w, with a pH of about 3.5 to 5.1.

27. The method as defined in claim 18 wherein the hafnium ion concentration in the rinse solution is about 0.0008 to 0.0010% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

28. The method as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the zirconium concentration is about 0.00065 to 0.0011% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

29. The method as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the hafnium concentration is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

30. A rinse solution as defined in claim 18 wherein the hafnium ion concentration in the rinse solution is about 0.00035 to 0.0050% w/w and the zirconium concentration is about 0.00065 to 0.0011% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

31. A rinse solution as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.0016% w/w and the zirconium concentration is about 0.00065 to 0.0011% w/w and the hafnium ion concentration is about 0.00035 to 0.0050% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1.

32. A rinse solution as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.001% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1, where the solution is applied by means of spraying.

33. A rinse solution as defined in claim 18 wherein the titanium ion concentration in the rinse solution is about 0.00035 to 0.001% w/w and the phenolic resin concentration is about 0.01 to 0.077% w/w, with a pH of about 4.0 to 5.1, where the solution is applied by means of dipping.

34. The method as defined in claim 18 wherein the Group IVA metal ion is from a Group IVA metal ion source selected from the group consisting of hexafluorozirconic acid, hexafluorotitanic acid, hafnium oxide, titanium oxysulfate, titanium tetrafluoride, zirconium sulfate and mixtures thereof.

35. The method as defined in claim 18 wherein the Group IVA metal ion concentration is about 0.00035 to 0.0050% w/w.

37. The method as defined in claim 18 wherein the phenolic resin is a mixture of substituted phenol compounds, selected from the group consisting of 2-hydroxybenzyl alcohol, 4-hydroxybenzyl alcohol, 2,6-dimethylol phenol, 2,4-dimethylol phenol and 2,4,6-trimethylol phenol.