Abstract Aqueous polymer dispersions useful for coating substrates are prepared by polymerization of olefinically unsaturated monomers in aqueous medium in the presence of radical formers and hydrophilically modified, urethane-group-containing emulsifiers having an average molecular weight below 30,000, wherein the urethane-group-containing emulsifiers are oligourethanes having a branched molecular structure which (i) are produced from organic polyisocyanates and organic compounds containing isocyanate-reactive groups with the reactants containing hydrophilic groups or groups convertible into hydrophilic groups and which are monofunctional or difunctional to isocyanate addition reaction, with the molar ratio of monofunctional hydrophilic components to the corresponding difunctional components being at least 2:1, and which (ii) have a content of chemically incorporated hydrophilic groups sufficient to impart the oligourethane solubility or dispersibility in water, with the proviso that, on a statistical average, at least 2.2 terminally incorporated hydrophilic groups are present per molecule.
A process for the production of aqueous dispersions of polymers by polymerization of olefinically unsaturated monomers in aqueous medium in the presence of radical formers and hydrophilically modified, urethane-group-containing emulsifiers having an average molecular weight below 30,000 wherein the urethane-group-containing emulsifiers are oligourethanes having a branched molecular structure which (i) are produced from the reaction of (a) organic polyisocyanates, (b) organic compounds containing isocyanate-reactive groups and (c) organic compounds containing hydrophilic groups or functional groups which are converted into hydrophilic groups by neutralization or quaternization after the isocyanate polyaddition reaction wherein the compounds (c) are monofunctional or a mixture of monofunctional are difunctional compounds relative to the isocyanate addition reaction, with the molar ratio in said mixture of monofunctional hydrophilic reactants to the corresponding difunctional reactants being at least 2:1, and which (ii) have a content of chemically incorporated hydrophilic groups sufficient to impart to the oligourethane solubility or dispersibility in water, with the proviso that, on a statistical average at least 2.2 terminally incorporated hydrophilic groups are present per molecule.
Claim 2
Dependent Claim
171 words
A process for the production of aqueous dispersions of polymers by polymerization of olefinically unsaturated monomers in aqueous medium in the presence of radical formers and hydrophilically modified, urethane-group-containing emulsifiers having an average molecular weight below 30,000 wherein the urethane-group-containing emulsifiers are oligourethanes having a branched molecular structure which (i) are produced from the reaction of (a) organic polyisocyanates, (b) organic compounds containing isocyanate-reactive groups and (c) organic compounds containing hydrophilic groups or functional groups which are converted into hydrophilic groups by neutralization or quaternization after the isocyanate polyaddition reaction wherein the compounds (c) are monofunctional or a mixture of monofunctional are difunctional compounds relative to the isocyanate addition reaction, with the molar ratio in said mixture of monofunctional hydrophilic reactants to the corresponding difunctional reactants being at least 2:1, and which (ii) have a content of chemically incorporated hydrophilic groups sufficient to impart to the oligourethane solubility or dispersibility in water, with the proviso that, on a statistical average at least 2.2 terminally incorporated hydrophilic groups are present per molecule.
Claim 3
Dependent Claim
23 words
A process as claimed in claim 1 wherein the oligourethanes contain 2 to 400 milliequivalents per 100 grams of terminally incorporated carboxylate groups.
Claim 4
Dependent Claim
26 words
A process as claimed in claim 1 wherein the ratio by weight of the olefinically unsaturated monomers to the oligourethane emulsifiers is from 1:1 to 99:1.
Claim 5
Dependent Claim
31 words
A process as claimed in claim 1 wherein the polymerization reaction is carried out noncontinously, continously or by the feed process at temperatures in the range from 10° to 50° C.
Claim 6
Dependent Claim
9 words
Dispersions produced by the process claimed in claim 1.