초록 ▼

A process is disclosed for performing encapsulation, en masse, by an in situ polymerization reaction to yield capsule wall material. The reaction comprises the polymerization of urea and formaldehyde, or monomeric or low molecular weight polymers of dimethylol urea or methylated dimethylol urea, mel

A process is disclosed for performing encapsulation, en masse, by an in situ polymerization reaction to yield capsule wall material. The reaction comprises the polymerization of urea and formaldehyde, or monomeric or low molecular weight polymers of dimethylol urea or methylated dimethylol urea, melamine and formaldehyde, monomeric or low molecular weight polymers of methylol melamine or methylated methylol melamine, in an aqueous vehicle and the reaction is conducted in the presence of certain acrylic acid copolymers. The disclosed encapsulation process provides improved resistance of the emulsion of intended capsule core material to destabilization and permits the manufacture of microcapsules with improved drop size distribution, improved resistance to frictional smudge damage and enhanced impermeability.

대표청구항 ▼

1. A process for preparing microcapsules in an aqueous manufacturing vehicle which comprises enwrapping particles of intended capsule core material, substantially insoluble in said vehicle, with polymeric shells produced by in situ polymerization of melamine and formaldehyde, methylol melamine, meth

1. A process for preparing microcapsules in an aqueous manufacturing vehicle which comprises enwrapping particles of intended capsule core material, substantially insoluble in said vehicle, with polymeric shells produced by in situ polymerization of melamine and formaldehyde, methylol melamine, methylated methylol melamine, urea and formaldehyde, dimethylol urea or methylated dimethylol urea in the presence of an acrylic acid-alkyl acrylate copolymer, wherein the weight percent and type of alkyl acrylate in said copolymer are selected from the group consisting of about 12 to about 30 ethyl acrylate, about 6 to about 14 propyl acrylate, about 4 to about 20 butyl acrylate, about 2 to about 14 amyl acrylate, about 2 to about 10 hexyl acrylate, about 4 to about 12 cyclohexyl acrylate and about 2 2-ethylhexyl acrylate and said copolymer is present as about 0.4 to about 15 percent by weight of said manufacturing vehicle. 2. The process of claim 1 wherein the polymeric shell is produced by in situ polymerization of methylated methylol melamine or urea and formaldehyde. 3. The process of claim 1 wherein the polymeric shell is produced by in situ polymerization of methylated methylol melamine. 4. The process of claims 1, 2 or 3, wherein the polymerization is conducted at a temperature of about 40° C. to about 95° C. 5. The process of claim 4 wherein the polymerization is conducted at a temperature of about 50° C. to about 70° C. 6. The process of claim 5 wherein said copolymer consists of about 6 to about 10 weight percent butyl acrylate. 7. The process of claim 6 wherein said copolymer consists of about 8 weight percent butyl acrylate. 8. The process of claim 5 wherein said copolymer consists of about 18 to about 24 weight percent ethyl acrylate. 9. The process of claim 8 wherein said copolymer consists of about 22 weight percent ethyl acrylate. 10. The process of claim 5 wherein said copolymer consists of about 2 to about 6 weight percent hexyl acrylate. 11. The process of claim 10 wherein said copolymer consists of about 4 weight percent hexyl acrylate. 12. The process of claim 5 wherein said copolymer consists of about 4 to about 6 weight percent cyclohexyl acrylate. 13. The process of claim 12 wherein said copolymer consists of about 4 weight percent cyclohexyl acrylate. 14. Microcapsules produced by a process as claimed in claim 1.