Method for the passivation of metal surfaces with polymers containing acid groups
Process for the passivation of metallic surfaces by treatment of the surface with an acidic, aqueous preparation which comprises at least one water-soluble acid group-containing polymer and Zn, Ca, Mg or Al ions, said process being in particular a continuous process for the passivation of strip metals.
1. A process for the passivation of a metallic surface which comprises treating the metallic surface with an acidic, aqueous formulation comprising at least one water-soluble polymer X comprising acidic groups and at least one metal ion, wherein
the polymer has at least 0.6 mol of acid groups/100 g of the polymer,
the pH of the formulation is from 0.5 to 3.5,
the amount of the polymer is from 5 to 40% by weight, based on the amount of all components of the formulation,
the metal ion is at least one selected from the group consisting of Zn2+, Ca2+, Mg2+ and A13+, and
the amount of metal ions is from 0.01% by weight to 25% by weight, based on the total amount of all polymers X, wherein the passivation is a chromium and fluoride free passivation and there are no ions of nickel, of manganese and of cobalt are used in the process.
2. The process according to claim 1 , wherein the formulation furthermore comprises phosphate ions.
3. The process according to claim 1 , wherein the formulation furthermore comprises methanesulfonate ions.
4. The process according to claim 1 , wherein the water-soluble polymer X is a copolymer X1 which is composed of the following monomeric units-based in each case on the amount of all monomers incorporated as polymerized units in the copolymer:
(A) from 40 to 90% by weight of (meth)acrylic acid,
(B) from 10 to 60% by weight of at least one further monoethylenically unsaturated monomer which differs from (A) and has one or more acidic groups, and
(C) optionally from 0 to 30% by weight of at least one further ethylenically unsaturated monomer differing from (A) and (B).
5. The process according to claim 4 , wherein the monomers (B) are monomers
(B1) monoethylenically unsaturated dicarboxylic acids having 4 to 7 carbon atoms or
(B2) monoethylenically unsaturated phosphoric and/or phosphonic acids or a mixture of (B1) and (B2).
6. The process according to claim 5 , wherein the copolymer comprises at least one monomer (B1) and at least one monomer (B2).
7. The process according to claim 6 , wherein the amount of the monomers (A) is from 50 to 90% by weight, the amount of (B1) is from 5 to 45% by weight, the amount of (B2) is from 5 to 45% by weight and the amount of (C) is from 0 to 20% by weight.
8. The process according to claim 6 , wherein the amount of the monomers (A) is from 50 to 80% by weight, the amount of (B1) is from 12 to 42% by weight, the amount of (B2) is from 8 to 38% by weight and the amount of (C) is from 0 to 10% by weight.
9. The process according to claim 5 , wherein (B1) is maleic acid and (B2) is vinylphosphonic acid.
10. The process according to claim 1 , wherein the formulation furthermore comprises from 0.01% to 70% by weight of at least one dispersed wax, based on the polymer X.
11. The process according to claim 1 , wherein the metallic surface is one comprising Zn, Mg, Al, Sn, Fe, Ni or alloys thereof.
12. The process according to claim 1 , wherein the metal surface is the surface of a strip metal.
13. The process according to claim 12 , wherein the strip metal is electrogalvanized or hot-galvanized steel.
14. The process according to claim 1 , wherein the treatment is carried out by means of a continuous process.
15. The process according to claim 1 , wherein the amount of the polymer to 2 to 35% by weight based on the weight of all components in the formulation.
16. The process according to claim 1 , wherein the amount of the polymer to 5 to 25% by weight based on the weight of all components in the formulation.
17. The process according to claim 1 , wherein the degree of neutralization of the acid groups in the polymer to not more than 40%.
18. The process according to claim 1 , wherein the degree of neutralization of the acid groups in the polymer from 0 to 30 mol %.
19. The process according to claim 1 , wherein the degree of neutralization of the acid groups in the polymer from 0 to 20 mol %.
20. The process according to claim 1 , wherein the degree of neutralization of the acid groups in the polymer from 2 to 10 mol %.