# US 4,393,171 A · Process for preparing rubbery polymer reinforced styrenic resins > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 4,393,171 A - Document ID: US4393171A - Status: Granted - Kind: A - Application number: 06/238,414 - Filed: 1981-02-26 - Granted: 1983-07-12 - Earliest claimed: 1981-02-26 - Assignees: Labofina, S.A. - Inventors: William J. I. Bracke; Emmanuel Lanza - Web page: https://patentgrep.com/patent/US4393171A ## CPC - C08F 257/02: on to polymers of styrene or alkyl-substituted styrenes - C08F 265/08: on to polymers of nitriles - C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS ## Abstract A continuous mass polymerization process for preparing rubber reinforced styrenic copolymers comprising forming a solution in an inert solvent of a styrenic polymer matrix and a monomer material capable of polymerizing to form a cross-linked rubbery polmyer, continuously charging the solution into a polymerization reactor and subjecting the solution to mass polymerization conditions whereby there is formed in situ a cross-linked rubbery polymer dispersed in the styrenic polymer matrix, continuously withdrawing the reaction mixture from the polymerization reactor and recovering the resulting rubber reinforced styrenic copolymer. ## Claims ### Claim 1 A process for continuous preparation of a rubbery polymer material reinforced styrenic resin comprising the steps of: a. adding a monomer material selected from the group consisting of alkyl esters of acrylic acid, alkyl esters of methacrylic acid and mixtures thereof, together with a polyfunctional cross-linking agent to a first solution of a copolymeric matrix of a styrenic compound and an acrylonitrile compound in an inert solvent, whereby there is formed a second solution of monomer material, polyfunctional cross-linking agent and said copolymeric matrix in said inert solvent; b. continuously charging said second solution into a polymerization zone and subjecting said second solution in said polymerization zone to mass polymerization conditions to polymerize said monomer material whereby there is formed in situ a cross-linked rubbery material dispersed in said copolymeric matrix; c. continuously withdrawing the reaction mixture from said polymerization zone and continuously charging the withdrawn mixture into a devolatilization zone to remove the inert solvent and any residual monomer material, and d. recovering a rubbery polymer material reinforced styrenic resin wherein the rubbery material formed in situ is highly dispersed in the copolymer matrix. ### Claim 2 (depends on 1) A process according to claim 1, wherein the styrenic polymer matrix comprises a copolymer of from about 10 to about 90 weight percent styrenic compound and about 90 to about 10 weight percent acrylonitrile. ### Claim 3 (depends on 2) A process according to claim 2, wherein the weight ratio of styrenic compound to acrylonitrile comprises between about 4:1 and about 1:1. ### Claim 4 (depends on 2) A process according to claim 2, wherein the copolymeric matrix comprises a minor amount of a rubbery polymer not exceeding about 8% by weight. ### Claim 5 (depends on 1) A process according to claim 1, wherein the solution of copolymeric matrix in the inert solvent comprises from about 10 to about 70 weight % of copolymeric matrix. ### Claim 6 (depends on 5) A process according to claim 5, wherein the solution contains from about 20 to about 50 weight % of copolymeric matrix. ### Claim 7 (depends on 1) A process according to claim 1, wherein the monomer material is a saturated alkyl ester wherein the alkyl group contains from 1 to 14 carbon atoms. ### Claim 8 (depends on 7) A process according to claim 7, wherein the monomer material produces a rubbery material having a glass-transition temperature lower than about 0.degree. C. ### Claim 9 (depends on 7) A process according to claim 7, wherein the amount of monomer material comprises between about 15 and 50%, based on the total weight of the copolymeric matrix and monomer material. ### Claim 10 (depends on 1) A process according to claim 1, wherein the cross-linking agent is selected from the group consisting of alkenyl esters of lower aliphatic carboxylic acids, acrylates of polyol compounds, methacrylates of polyol compounds and mixtures thereof. ### Claim 11 (depends on 10) A process according to claim 10, wherein the amount of cross-linking agent comprises between about 0.025% and about 5%, based on the weight of the monomer material. ### Claim 12 (depends on 1) A process according to claim 1, wherein the inert solvent is a saturated solvent having a boiling point between about 120.degree. and about 175.degree. C. ### Claim 13 (depends on 12) A process according to claim 12, wherein the saturated solvent has a boiling point between about 130.degree. and about 150.degree. C. ### Claim 14 (depends on 12) A process according to claim 12, wherein the solvent is an alkylbenzene. ### Claim 15 (depends on 14) A process according to claim 14, wherein the solvent is ethylbenzene. ### Claim 16 (depends on 1) A process according to claim 1, wherein the mass polymerization is a thermal polymerization and is carried out at a temperature between about 130.degree. and about 170.degree. C. ### Claim 17 (depends on 1) A process according to claim 1, wherein the mass polymerization is carried out in the presence of a free radical generating catalyst at a temperature between about 120.degree. and about 140.degree. C. ### Claim 18 A continuous mass polymerization process for preparing rubbery polymer reinforced styrenic copolymer resins comprising the steps of: a. forming a solution in an inert solvent comprising a styrenic polymer matrix and a monomer material capable of polymerizing to form a cross-linked rubbery polymer material; b. continuously charging said solution from step a. into a polymerization reactor and subjecting said solution to mass polymerization conditions to mass polymerize said monomer material whereby there is formed in situ a cross-linked rubbery polymer material dispersed in the styrenic polymer matrix; c. continuously withdrawing the reaction mixture from step b. from said polymerization reactor; and d. recovering a rubbery polymer reinforced styrenic copolymer resin from the withdrawn reaction mixture from step c. ### Claim 19 (depends on 18) A process according to claim 18 wherein said styrenic polymer matrix is selected from the group consisting of styrene homopolymers, copolymers of styrene and acrylonitrile; copolymers of styrene, acrylonitrile and butadiene; copolymers of styrene and butadiene; and copolymers of styrene and methyl methacrylate. ### Claim 20 (depends on 18) A process according to claim 18 wherein said styrenic polymer matrix is a copolymer of styrene and at least one other ethylenically unsaturated monomer. ### Claim 21 (depends on 20) A process according to claim 20 wherein said copolymer is a styrene-acrylonitrile copolymer. ### Claim 22 (depends on 18) A process according to claim 18 wherein said monomer material comprises at least one monomer selected from the group consisting of acrylate monomers and conjugated diolefins. ### Claim 23 (depends on 22) A process according to claim 22 wherein said monomer material comprises an alkyl ester of acrylic acid or methacrylic acid and an effective polyfunctional cross-linking amount of at least one cross-linking agent. ### Claim 24 (depends on 23) A process according to claim 23 wherein said alkyl ester is selected from the group consisting of n-butyl acrylate and 2-ethylhexyl acrylate. ### Claim 25 (depends on 22) A process according to claim 22 wherein said monomer material comprises a conjugated diolefin. ### Claim 26 (depends on 25) A process according to claim 25 wherein said conjugated diolefin is 1,3-butadiene. ### Claim 27 (depends on 18) A process according to claim 18 wherein said recovery step comprises treating the mixture withdrawn from the polymerization reactor to remove the inert solvent and any residual monomer material which may be present therein. ### Claim 28 (depends on 27) A process according to claim 27 wherein said mixture is devolatilized in a vacuum chamber to remove the inert solvent and any residual monomer material. ### Claim 29 (depends on 27) A process according to claim 27 wherein a film of said mixture is heated to remove the inert solvent and any residual monomer material. ### Claim 30 (depends on 18) A process according to claim 18 wherein said inert solvent is a saturated alkylaromatic compound. ### Claim 31 (depends on 30) A process according to claim 30 wherein said saturated alkylaromatic compound is ethylbenzene. ### Claim 32 (depends on 18) A process according to claim 18 wherein the initial solution is formed by mass polymerization of a mixture of styrene and acrylonitrile in an inert solvent to produce a styrene-acrylonitrile copolymer matrix in solution in said solvent, said matrix being substantially free of reactive sites; and thereafter adding said monomer material to the copolymer matrix solution. ### Claim 33 (depends on 18) A process according to claim 18 wherein said mass polymerization is effected at a temperature lying in the range from about 100.degree. C. to about 170.degree. C. ### Claim 34 (depends on 18) A process according to claim 18 wherein said mass polymerization is effected in the substantial absence of molecular oxygen and in the presence of at least one free radical generating catalyst. ### Claim 35 (depends on 34) A process according to claim 34 wherein said mass polymerization is effected at a temperature lying in the range between about 100.degree. C. and about 140.degree. C. ### Claim 36 (depends on 18) A process according to claim 18 wherein said mass polymerization is a thermal polymerization. ### Claim 37 (depends on 36) A process according to claim 36 wherein said mass polymerization is effected at a temperature lying in the range from about 120.degree. C. to about 170.degree. C. ### Claim 38 (depends on 18) A process according to claim 18 wherein said rubbery polymer reinforced styrenic copolymer resin is substantially gel-free. ### Claim 39 (depends on 18) A process according to claim 18 wherein said monomer material is selected from the group consisting of acrylic acid esters, mixtures of acrylic acid esters, and mixtures of a methacrylic acid ester with at least one acrylic acid ester. ### Claim 40 (depends on 39) A process according to claim 39 wherein said monomer material further comprises an effective cross-linking amount of at least one polyfunctional cross-linking agent. ### Claim 41 (depends on 18) A process according to claim 18 wherein said styrenic polymer matrix is substantially free of reactive sites. ### Claim 42 (depends on 18) A process according to claim 18 wherein said monomer material is substantially uniformly dispersed throughout said styrenic polymer matrix in said solution. ### Claim 43 A continuous mass process for preparing rubbery polymer reinforced ASA styrenic resins comprising the steps of: a. forming a solution in an inert solvent of a styrene-acrylonitrile copolymer matrix together with an acrylate monomer and a polyfunctional cross-linking agent; b. continuously charging said solution into a polymerization zone and subjecting it to mass polymerization whereby there is formed in situ a cross-linked rubbery material dispersed in the styrene-acrylonitrile matrix, c. continuously withdrawing the reaction mixture from the polymerization zone and charging it into a devolatilization zone; and d. recovering the resulting rubbery polymer reinforced ASA styrenic resin.