Process for forming an aqueous polymeric dispersion
AssigneeRohn and Haas Company
InventorsJames Keith Bardman, William Christopher Finch, Robert Mitchell Blankenship
Life of this patent
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Abstract
A process for forming certain aqueous polymeric dispersions including a first emulsion polymer having an average particle diameter of 150 to 3000 nanometers and a second emulsion polymer having an average particle diameter of 40 to 600 nanometers where at least the first emulsion polymer particles, when dry, contain at least one void is provided. Also provided are the aqueous polymeric dispersions made by the process and paper or paperboard coatings and paints including the aqueous polymeric dispersions.
Claims5
A process for forming an aqueous polymeric dispersion comprising
- (1) forming emulsion-polymerized multistaged first polymer particles comprising
- (a) a hydrophilic core polymer formed from 5% to 100% by weight, based on the total weight of said core polymer, of a hydrophilic monoethylenically unsaturated monomer and from 0% to 95% by weight, based on the total weight of said core polymer, of at least one nonionic monoethylenically unsaturated monomer;
- (b) a first shell polymer formed from 90% to 99.9% by weight, based on the total weight of said first shell polymer, of at least one nonionic monoethylenically unsaturated monomer and from 0.1% to 10% by weight, based on the total weight of said first shell polymer, of an acid functional monoethylenically unsaturated monomer, wherein said first shell polymer fully encapsulates said core polymer, wherein the ratio of the weight of said core polymer to the weight of said first shell polymer is from 1:2 to 1:100, and wherein said first shell polymer has a glass transition temperature greater than 50° C.;
- and
- (c) a second shell polymer formed from 93% to 99.9% by weight, based on the total weight of said second shell polymer, of at least one nonionic monoethylenically unsaturated monomer and from 0.1% to 7% by weight, based on the total weight of said second shell polymer, of an acid functional monoethylenically unsaturated monomer, wherein said second shell polymer is formed in the presence of said first shell polymer, and wherein said second shell polymer has a glass transition temperature from 10° C. to −50° C., and wherein said second shell polymer is at least 10% by weight of the total weight of said first shell polymer and said second shell polymer;
- (2) forming a second emulsion polymer in the presence of said first emulsion polymer by
- (a) adding, after 2% by weight of said core polymer has been formed, an amount of surfactant sufficient to generate new particles or an emulsion-polymerized seed latex having a particle diameter less than 200 nanometers to the polymerization;
- (b) then adding any remainder of said first shell polymer monomer mixture and then any remainder of said second shell polymer monomer mixture and from 0 to 90% by weight, based on the weight of the solids of said aqueous polymeric dispersion, of at least one ethylenically unsaturated monomer;
- (3) effecting polymerization of at least 95% of all added monomer by weight based on the weight of the solids of said aqueous polymeric dispersion;
- and
- (4) neutralizing said aqueous dispersion formed with a base so as to swell said core and form particles which, when dry, contain a void.
A process for forming an aqueous polymeric dispersion comprising
- (1) forming a first emulsion polymer comprising particles formed from at least one ethylenically unsaturated monomer;
- (2) forming a multistaged second emulsion polymer comprising
- (a) a hydrophilic core polymer formed from 5% to 100% by weight, based on the total weight of said core polymer, of a hydrophilic monoethylenically unsaturated monomer and from 0% to 95% by weight, based on the total weight of said core polymer, of at least one nonionic monoethylenically unsaturated monomer;
- (b) a first shell polymer formed from 90% to 99.9% by weight, based on the total weight of said first shell polymer, of at least one nonionic monoethylenically unsaturated monomer and from 0.1% to 10% by weight, based on the total weight of said first shell polymer, of an acid functional monoethylenically unsaturated monomer, wherein said first shell polymer fully encapsulates said core polymer, wherein the ratio of the weight of said core polymer to the weight of said first shell polymer is from 1:2 to 1:100, and wherein said first shell polymer has a glass transition temperature greater than 50° C.;
- and
- (c) a second shell polymer formed from 93% to 99.9% by weight, based on the total weight of said second shell polymer, of at least one nonionic monoethylenically unsaturated monomer and from 0.1% to 7% by weight, based on the total weight of said second shell polymer, of an acid functional monoethylenically unsaturated monomer, wherein said second shell polymer is formed in the presence of said first shell polymer, and wherein said second shell polymer has a glass transition temperature from 10° C. to −50° C., and wherein said second shell polymer is at least 10% by weight of the total weight of said first shell polymer and said second shell polymer;
- and
- (3) effecting polymerization of at least 95% of all added monomer by weight based on the weight of the solids of said aqueous polymeric dispersion;
- and
- (4) neutralizing said aqueous dispersion formed with a base so as to swell said core and form second emulsion polymer particles which, when dry, contain a void.
Dependencies are inferred from the claim text.