Process for production of a multicoat coating

Claim 2

A process for the production of a multicoat protective and/or decorative coating on a substrate surface, the process comprising the stages of (1) a pigmented aqueous coating composition containing as the film-forming material a water-thinnable emulsion polymer is applied to the substrate surface as the basecoat coating composition (2) a polymeric film is formed from the composition applied in stage (1) (3) a transparent topcoat coating composition is applied to the basecoat obtained in this manner and subsequently (4) the basecoat together with the topcoat is dried at temperatures below 80° C., wherein the basecoat coating composition contains a water-thinnable emulsion polymer which is obtained in that (a) in the first stage 10 to 90 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers is polymerized in the aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the ethylenically unsaturated monomer or the mixture of ethylenically unsaturated monomers being chosen such that in the first stage a polymer having a glass transition temperature (T G1 ) of +30° to +110° C. is obtained, and (b) after at least 80% by weight of the ethylenically unsaturated monomer or mixture of monomers employed in the first stage have reacted, in a second type stage 90 to 10 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers are polymerized in the presence of the polymer obtained in the first stage, the monomer employed in the second stage or the mixture of ethylenically unsaturated monomers employed in the second stage being chosen such that a sole polymerization of the monomer employed in the second stage or of the mixture of ethylenically unsaturated monomers employed in the second stage gives rise to a polymer having a glass transition temperature (T G2 ) of -60° to +20° C., and the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular weight of 200,000 to 2,000,000, and the ethylenically unsaturated monomer or mixture of monomers employed in the first stage and the nature and amount of the ethylenically unsaturated monomer or mixture of monomers employed in the second stage being chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 mg of KOH/g and the difference T G1 -T G2 is 10° to 170° C.

Claim 3

The process as claimed in claim 1, wherein the basecoat coating composition comprises a metal pigment.

Claim 4

The process as claimed in claim 1, wherein the film-forming material comprises 100 to 40% by weight of the emulsion polymer and 0 to 60% by weight of a water-thinnable polyuret resin, the amounts in each case being based on the solids content and their total always being 100% by weight.

Claim 5

The process as claimed in claim 1 wherein in the first stage a mixture is used comprising: (a1) 100 to 60,% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters and (a2) 0 to 40,% by weight of a monomer which is copolymerizable with (a1) or a mixture of such monomers, the total of the weights of (a1) and (a2) being always 100% by weight.

Claim 6

The process as claimed in claim 1, wherein in the second stage a mixture is used comprising: (b1) 47 to 99,% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters (b2) 1 to 20,% by weight of a monomer which is copolymerizable with (b1), (b3) and (b4) and carries at least one hydroxyl group or a mixture of such monomers (b3) 0 to 8,% by weight of a monomer which is copolymerizable with (b1), (b2) and (b4) and carries at least one carboxyl or sulfonic acid group or a mixture of such monomers and (b4) 0 to 25,% by weight of a further monomer which is copolymerizable with (b1), (b2) and (b3) or a mixture of such monomers, the total of the weight of (b1), (b2), (b3) and (b4) always 100% by weight.

Claim 7

The process as claimed in claim 1, wherein the transparent topcoat coating composition comprises a hydroxyl-containing acrylate copolymer and a blocked diisocyanate and/or polyisocyanate.

Claim 8

A process for the production of a multicoat protective and/or decorative coating on a substrate surface in the automotive refinishing sector, the process comprising the stages of (1) a pigmented aqueous coating composition comprising as the film-forming material a water-thinnable emulsion polymer is applied to the substrate surface as a basecoat coating composition (2) a polymeric film is formed from the composition applied in stage (1) (3) a transparent topcoat coating composition is applied to the basecoat obtained in this manner and subsequently (4) the basecoat together with the topcoat is dried at temperatures below 100° C., wherein the basecoat coating composition contains a water-thinnable emulsion polymer which is obtained in that (a) in the first stage 10 to 90 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers is polymerized in the aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the ethylenically unsaturated monomer or the mixture of ethylenically unsaturated monomers being chosen such that in the first stage a polymer having a glass transition temperature (T G1 ) of +30° to +110° C. is obtained, and (b) after at least 80% be weight of the ethylenically unsaturated monomer or mixture of monomers employed in the first stage have reacted, in a second stage 90 to 10 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers are polymerized in the presence of the polymer obtained in the first stage, the monomer employed in the second stage or the mixture of ethylenically unsaturated monomers employed in the second stage being chosen such that a sole polymerization of the monomer employed in the second stage or of the mixture of ethylenically unsaturated monomers employed in the second stage gives rise to a polymer having a glass transition temperature (T G2 ) of -60° to +20° C., and the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular weight of 200,000 to 2,000,000, and the ethylenically unsaturated monomer or mixture of monomers employed in the first stage and the nature and amount of the ethylenically unsaturated monomer or mixture of monomers employed in the second stage being chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 mg of KOH/g and the difference T G2 -T G2 is 10° to 170° C.

Claim 9

A process for the production of a multicoat protective and/or decorative coating on a substrate surface in the automotive refinishing sector, the process comprising the stages of (1) a pigmented aqueous coating composition comprising as the film-forming material a water-thinnable emulsion polymer is applied to the substrate surface as a basecoat coating composition (2) a polymeric film is formed from the composition applied in stage (1) (3) a transparent topcoat coating composition is applied to the basecoat obtained in this manner and subsequently (4) the basecoat together with the topcoat is dried at temperatures below 100° C., wherein the basecoat coating composition contains a water-thinnable emulsion polymer which is obtained in that (a) in the first stage 10 to 90 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers is polymerized in the aqueous phase in the presence of one or more emulsifiers and one or more radical-forming initiators, the ethylenically unsaturated monomer or the mixture of ethylenically unsaturated monomers being chosen such that in the first stage a polymer having a glass transition temperature (T G1 ) of +30° to +110° C. is obtained, and (b) after at least 80% be weight of the ethylenically unsaturated monomer or mixture of monomers employed in the first stage have reacted, in a second stage 90 to 10 parts by weight of an ethylenically unsaturated monomer or a mixture of ethylenically unsaturated monomers are polymerized in the presence of the polymer obtained in the first stage, the monomer employed in the second stage or the mixture of ethylenically unsaturated monomers employed in the second stage being chosen such that a sole polymerization of the monomer employed in the second stage or of the mixture of ethylenically unsaturated monomers employed in the second stage gives rise to a polymer having a glass transition temperature (T G2 ) of -60° to +20° C., and the reaction conditions being chosen such that the resultant emulsion polymer has a number average molecular weight of 200,000 to 2,000,000, and the ethylenically unsaturated monomer or mixture of monomers employed in the first stage and the nature and amount of the ethylenically unsaturated monomer or mixture of monomers employed in the second stage being chosen such that the resultant emulsion polymer has a hydroxyl value of 2 to 100 mg of KOH/g and the difference T G2 -T G2 is 10° to 170° C.

Claim 10

The process as claimed in claim 7, wherein the basecoat is dried together with the topcoat at temperatures below 80° C.

Claim 11

The process as claimed in claim 7, wherein the basecoat coating composition comprises a metal pigment.

Claim 12

The process as claimed in claim 7, wherein the film-forming material comprises 100 to 40% by weight of the emulsion polymer and 0 to 60% by weight of a water-thinnable polyurethane resin, the amount in each case being based on the solids content and their total always being 100% by weight.

Claim 13

The process as claimed in claim 7, wherein in the first stage a mixture is used comprising (a1) 100 to 60, % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters and (a2) 0 to 40, % by weight of a monomer which is copolymerizable with (a1) or a mixture of such monomers, the total of the weights of (a1) and (a2) being always 100% by weight.

Claim 14

The process as claimed in claim 7, wherein in the second stage a mixture is used comprising (b1) 47 to 99, % by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters (b2) 1 to 20, % by weight of a monomer which is copolymerizable with (b1), (b3) and (b4) and carries at least one hydroxyl group or a mixture of such monomers (b3) 0 to 8, % by weight of a monomer which is copolymerizable with (b1), (b2) and (b4) and carries at least one carboxyl or sulfonic acid group or a mixture of such monomers and (b4) 0 to 25, % by weight of a further monomer which is copolymerizable with (b1), (b2) and (b3) or a mixture of such monomers, the total of the weight of (b1), (b2), (b3) and (b4) being always 100% by weight.

Claim 15

The process as claimed in claim 7, wherein the transparent topcoat coating composition comprises a hydroxyl-containing acrylate copolymer and a blocked diisocyanate and/or polyisocyanate.r86

Claim 16

The process as claimed in claim 1, wherein in the first stage a mixture is used comprising: (a1) 99.5 to 75% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters and (a2) 0.5 to 25% by weight of a monomer which is copolymerizable with (a1) or a mixture of such monomers, the total of the weights of (a1) and (a2) being always 100% by weight.

Claim 17

The process as claimed in claim 1, wherein in the second stage a mixture is used comprising: (b1) 75 to 90% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters (b2) 5 to 15% by weight of a monomer which is copolymerizable with (b1), (b3) and (b4) and carries at least one hydroxyl group or a mixture of such monomers (b3) 2 to 6% by weight of a monomer which is copolymerizable with (b1), (b2) and (b4) and carries at least one carboxyl or sulfonic acid group or a mixture of such monomers and (b4) 2 to 15% by weight of a further monomer which is copolymerizable with (b1), (b2) and (b3) or a mixture of such monomers, the total of the weight of (b1), (b2), (b3) and (b4) being always 100% by weight.

Claim 18

The process as claimed in claim 7, wherein in the first stage a mixture is used comprising (a1) 99.5 to 75% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters and (a2) 0.5 to 25% by weight of a monomer which is copolymerizable with (a1) or a mixture of such monomers, the total of the weights of (a1) and (a2) being always 100% by weight.

Claim 19

The process as claimed in claim 7, wherein in the second stage a mixture is used comprising (b1) 75 to 90% by weight of a cycloaliphatic or aliphatic ester of methacrylic acid or acrylic acid or a mixture of such esters (b2) 5 to 15% by weight of a monomer which is copolymerizable with (b1), (b3) and (b4) and carries at least one hydroxyl group or a mixture of such monomers (b3) 2 to 6% by weight of a monomer which is copolymerizable with (b1), (b2) and (b4) and carries at least one carboxyl or sulfonic acid group or a mixture of such monomers and (b4) 2 to 15% by weight of a further monomer which is copolymerizable with (b1), (b2) and (b3) or a mixture of such monomers, the total of the weight of (b1), (b2), (b3) and (b4) being always 100% by weight.

Claim 20

The process as claimed in claim 1, wherein the basecoat coating composition comprises an aluminum pigment.

Claim 21

The process as claimed in claim 7, wherein the basecoat coating composition comprises an aluminum pigment.