# US 5,708,082 A · Process for preparing a styrenic resin > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,708,082 A - Document ID: US5708082A - Status: Granted - Kind: A - Application number: 08/677,729 - Filed: 1996-07-08 - Granted: 1998-01-13 - Earliest claimed: 1996-07-08 - Assignees: Chi Mei Corporation - Inventors: Shao-Chiu Huang - Web page: https://patentgrep.com/patent/US5708082A ## CPC - C08F 265/04: on to polymers of esters - C08F 285/00: Macromolecular compounds obtained by polymerising monomers on to preformed graft polymers - C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS ## Abstract In a process for preparing a styrenic resin, a rubber graft copolymer (A) having a weight average particle size of 0.05-0.8 .mu.m by coagulation and drying of a rubber graft copolymer latex (a). The rubber graft copolymer latex (a) is made from graft polymerization of a vinyl aromatic monomer and a vinyl cyanide monomer in the presence of a butadienic rubber latex. The styrenic resin is then prepared by a continuous bulk or solution polymerization method. The method comprises continuously charging 80 to 45 parts by weight of a vinyl aromatic monomer, 15 to 50 parts by weight of a vinyl cyanide monomer, 0 to 40 parts by weight of a copolymerizable monomer (totally 100 parts by weight of monomers), 0.1 to 6 parts by weight of the rubber graft copolymer based on 100 parts by weight of monomers and 0.1 to 10 parts by weight of an acrylic-based copolymer (B) based on 100 parts by weight of monomers into a reactor; polymerizing them to a conversion of 40 to 90 wt %; and removing the unreacted monomers and volatile components from the polymerized mixture. The styrenic resin produced by the above process has suitable impact strength, good rigidity and hardness, and excellent appearance and semi-transparency. ## Claims ### Claim 1 A process for preparing a styrenic resin by a continuous bulk or solution polymerization method, said resin having a rubber content of 0.1 to 4.5 wt. % which process comprises: (i) continuously charging into a reactor a feed containing 80 to 45 parts by weight of a vinyl aromatic monomer, 15 to 50 parts by weight of a vinyl cyanide monomer, 0 to 40 parts by weight of a copolymerizable monomer, and 0.1 to 6 parts by weight of a powdery rubber graft copolymer (A), based on a total of 100 parts by weight of said monomers, wherein said powdery rubber graft copolymer (A) has a weight average particle size of 0.05-0.8 .mu.m and is prepared by coagulating and drying a rubber graft copolymer latex (a), wherein said rubber graft copolymer latex (a) is made from graft polymerization of vinyl aromatic monomer and vinyl cyanide monomer in the presence of dienic rubber latex; (ii) charging to said reactor 0.1 to 10 parts by weight of an acrylic-based copolymer (B) based on a total of 100 parts by weight of said monomers, wherein said acrylic-based copolymer (B) is rigid and soluble in said monomers and is prepared from at least one monomer selected from methyl methacrylate and acrylonitrile, and a vinyl aromatic monomer, and wherein said acrylic-based copolymer (B) is added to said feed in an amount sufficient to facilitate the introduction of the feed into the reactor by preventing agglomeration of said copolymer (A) and thereby improving the dispersion of said copolymer (A) in said feed; (iii) polymerizing said feed in the presence of said acrylic-based copolymer (B) to a conversion of 40 to 90 wt. %; and (iv) removing the unreacted monomers and volatile components from the polymerized mixture. ### Claim 2 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein the temperature of said bulk or solution polymerization is 80.degree. to 200.degree. C. and the pressure thereof is 1 to 5 kg/cm.sup.2. ### Claim 3 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein the retention time of said bulk or solution polymerization is 1 to 5 hours. ### Claim 4 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein an alkaline earth metal salt is used for coagulating rubber graft copolymer latex (a). ### Claim 5 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein the degree of grafting of said rubber graft copolymer (A) is 10 to 100% and the molecular weight of the grafted rigid copolymer of said rubber graft copolymer (A) ranges from 40,000 to 120,000. ### Claim 6 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein said vinyl aromatic monomer is styrene or .alpha.-methyl styrene. ### Claim 7 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein said copolymerizable monomer is a maleimide-based monomer. ### Claim 8 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein said acrylic-based copolymer (B) is methyl methacrylate-methyl acrylate. ### Claim 9 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein said acrylic-based copolymer (B) is styrene-acrylonitrile copolymer. ### Claim 10 (depends on 1) A process for producing a styrenic resin according to claim 1, wherein the acrylic-based copolymer (B) is prepared from 10 to 100 wt. % of said at least one monomer selected from methyl methacrylate and acrylonitrile, and 0 to 80 wt. % of said vinyl aromatic monomer.