Process for forming a protective coating on zinciferous metal surfaces

• US 5,873,952 A
• Filed: 07/17/1997
• Issued: 02/23/1999
• Est. Priority Date: 08/20/1996
• Status: Expired due to Fees

• Current Assignee: Henkel Corporation (Henkel AG & Co KGaA)
• Original Assignee: Henkel Corporation (Henkel AG & Co KGaA)
• Inventors: Hall, James R., Prescott, Thomas J.
• Primary Examiner(s): Simmons, David A.
• Assistant Examiner(s): Koehler, Robert R.
• Application Number:
  US08/896,238
• Time in Patent Office: 586 Days
• Field of Search: 148/247, 148/273, 148/279
• US Class Current: 148/247
• CPC Class Codes: C23C 22/34 containing fluorides or complex fluorides
• CPC Class Codes: C23C 22/86 Regeneration of coating baths

Abstract

More nearly consistent quality of the coatings formed by contacting a zinciferous surface with an aqueous liquid treatment composition comprising water, transition metal cations, and fluorometallate anions, and, optionally, acidity adjustment agents can be achieved by (I) measuring the pH value of and the concentrations of transition metal cations and of fluorometallate anions in the treatment composition as it is used, (II) removing a specified fraction of the treatment composition from contact with the remainder of the treatment composition, and (III) adding one or more suitable replenisher compositions to the treatment composition, in order to maintain the measured pH and concentration values within specified ranges.

Claims

1. A process of forming, over a specified period of time, a protective coating on one or more zinciferous surface(s) by contacting the surface(s) with at least a portion of a specified total volume of an aqueous liquid treatment composition comprising water, transition metal cations, and fluorometallate anions, said process including steps of:

(I) measuring a pH value of, a transition metal cations concentrations in, and a fluorometallate anions concentrations in, the specified total volume of treatment composition as it is used;

(II) at at least one specified time after beginning use of the specified total volume of the treatment composition, said specified time being within said specified period of time over which the process is operated and being not more than 200 minutes, and, if the specified period of time is at least 400 minutes, also at one or more successive times thereafter, removing a specified fraction of the total volume of the treatment composition from contact with the remainder of the total volume of the treatment composition, said one or more successive times thereafter being selected so that not more than 200 minutes elapses between any such successive time and a most nearly preceding time at which a specified total fraction of the specified total volume of the treatment composition has been removed from contact with the remainder of the specified total volume of the treatment composition, said specified fraction or fractions of the specified total volume of the treatment being selected so that a ratio of said specified period of time, measured in hours, to a sum of all said specified fraction or fractions of the specified total volume that are removed from contact with the remainder of the specified total volume during said period of time has a numerical value not greater than 100; and

(III) adding one or more suitable replenisher compositions to the treatment composition, in order to maintain the pH value of the composition, the transition metal cations concentration of the composition, and the fluorometallate anions concentrations of the composition within respectively specified ranges for each of the pH value, the transition metal cations concentration, and the fluorometallate anions concentration.

2. A process according to claim 1, wherein the aqueous liquid treatment composition has a pH value from about 2.5 to about 5.0, a concentration of transition metal cations that is from about 0.0004 to about 0.050 M/L, a concentration of fluorometallate anions that is from about 0.001 to about 0.20 M/L, and a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in the same units, that is from about 0.50:

1.0 to about 10;

1.0.

3. A process according to claim 2, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 0.5:

1.0 to about 10;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.25;

1.0 to about 10;

1.0.

4. A process according to claim 3, wherein the aqueous liquid treatment composition has a pH value from about 2.9 to about 5.0, a concentration of transition metal cations that is from about 0.0008 to about 0.050 M/L, a concentration of fluorometallate anions that is from about 0.002 to about 0.10 M/L, a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in M/L, that is from about 0.80:

1.0 to about 8.0;

1.0, and a concentration of sulfuric acid that corresponds stoichiometrically to a concentration of sulfate ions that is greater than zero but not more than 0.40% of the total composition, and the zinciferous surface is immersed in a volume of aqueous liquid treatment composition in order to contact it.

5. A process according to claim 4, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 0.80:

1.0 to about 8.0;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.40;

1.0 to about 7.0;

1.0.

6. A process according to claim 5, wherein the aqueous liquid treatment composition has a pH value from about 3.1 to about 4.8, a concentration of transition metal cations that is from about 0.0015 to about 0.030 M/L, a concentration of fluorometallate anions that is from about 0.004 to about 0.070 M/L, a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in M/L, that is from about 1.20:

1.0 to about 5.0;

1.0, and a concentration of sulfuric acid that corresponds stoichiometrically to a concentration of sulfate ions that is greater than zero but not more than 0.36% of the total composition.

7. A process according to claim 6, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 1.00:

1.0 to about 6.0;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.50;

1.0 to about 6.0;

1.0.

8. A process according to claim 7, wherein the aqueous liquid treatment composition has a pH value from about 3.3 to about 4.6, a concentration of transition metal cations that is from about 0.0020 to about 0.020 M/L, a concentration of fluorometallate anions that is from about 0.006 to about 0.040 M/L, a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in M/L, that is from about 1.60:

1.0 to about 4.0;

1.0, and a concentration of sulfuric acid that corresponds stoichiometrically to a concentration of sulfate ions that is greater than zero but not more than 0.32% of the total composition.

9. A process according to claim 8, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 1.20:

1.0 to about 5.0;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.60;

1.0 to about 4.0;

1.0.

10. A process according to claim 9, wherein the aqueous liquid treatment composition has a pH value from about 3.5 to about 4.4, a concentration of transition metal cations that is from about 0.0020 to about 0.015 M/L, a concentration of fluorometallate anions that is from about 0.0070 to about 0.035 M/L, a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in M/L, that is from about 1.80:

1.0 to about 4.0;

1.0, and a concentration of sulfuric acid that corresponds stoichiometrically to a concentration of sulfate ions that is greater than zero but not more than 0.30% of the total composition.

11. A process according to claim 10, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 1.40:

1.0 to about 4.0;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.70;

1.0 to about 3.0;

1.0.

12. A process according to claim 11, wherein the aqueous liquid treatment composition has a pH value from about 3.60 to about 4.4, a concentration of transition metal cations that is from about 0.0030 to about 0.0100 M/L, a concentration of fluorometallate anions that is from about 0.0090 to about 0.022 M/L, a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in M/L, that is from about 2.10:

1.0 to about 3.20;

1.0, and a concentration of sulfuric acid that corresponds stoichiometrically to a concentration of sulfate ions that is greater than zero but not more than 0.26% of the total composition.

13. A process according to claim 12, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 1.70:

1.0 to about 3.20;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.85;

1.0 to about 2.0;

1.0.

14. A process according to claim 13, wherein the aqueous liquid treatment composition has a pH value from about 3.80 to about 4.20, a concentration of transition metal cations that is from about 0.0042 to about 0.0057 M/L, a concentration of fluorometallate anions that is from about 0.0105 to about 0.0125 M/L, a ratio of the concentration of fluorometallate anions to the concentration of transition metal cations, both measured in M/L, that is from about 2.40:

1.0 to about 2.80;

1.0, and a concentration of sulfuric acid that corresponds stoichiometrically to a concentration of sulfate ions that is greater than zero but not more than 0.20% of the total composition.

15. A process according to claim 14, wherein at least one replenisher composition added during step (III) comprises water, a molar concentration of transition metal cations, a molar concentration of fluorometallate anions, and a molar concentration of sulfuric acid, all of said molar concentrations having values such that the molar concentration of fluorometallate anions has a ratio to the molar concentration of transition metal cations that is from about 1.95:

1.0 to about 2.20;

1.0 and the molar concentration of sulfuric acid has a ratio to the molar concentration of fluorometallate ions that is from about 0.95;

1.0 to about 1.20;

1.0.

16. A process according to claim 15, wherein the transition metal cations are selected from the group consisting of nickel, cobalt, copper, iron, and manganese and the fluorometallate anions are selected from the group consisting of fluoroborate, fluorosilicate, fluorotitanate, and fluorozirconate anions.

17. A process according to claim 16, wherein the transition metal cations are selected from the group consisting of nickel, cobalt, and iron and the fluorometallate anions are selected from the group consisting of fluorotitanate and fluorozirconate anions.

18. A process according to claim 17, wherein the transition metal cations are nickel and the fluorometallate anions are fluorotitanate anions.

19. A process according to claim 1, wherein the transition metal cations are selected from the group consisting of nickel, cobalt, copper, iron, and manganese and the fluorometallate anions are selected from the group consisting of fluoroborate, fluorosilicate, fluorotitanate, and fluorozirconate anions.

20. A process according to claim 19, wherein the transition metal cations are selected from the group consisting of nickel, cobalt, and iron and the fluorometallate anions are selected from the group consisting of fluorotitanate and fluorozirconate anions.