Method of preparing abs graft copolymer and method of preparing thermoplastic resin composition
US-2020140597-A1 · May 7, 2020 · US
US12492277B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12492277-B2 |
| Application number | US-202117771679-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 22, 2021 |
| Priority date | Sep 18, 2020 |
| Publication date | Dec 9, 2025 |
| Grant date | Dec 9, 2025 |
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Disclosed is a method of preparing a graft copolymer and a method of preparing a thermoplastic resin composition including the prepared graft copolymer. Also disclosed is a method of preparing a graft copolymer including a process of adding an aromatic vinyl monomer and a vinyl cyanide monomer to a conjugated diene rubber latex that is enlarged with a polymer particle diameter control agent that has a specific glass transition temperature and an average particle diameter in a specific ratio to an average particle diameter of a conjugated diene rubber latex, and graft-polymerizing the same; and a method of preparing a thermoplastic resin composition including the prepared graft copolymer. Also disclosed is a graft copolymer prepared using the conjugated diene rubber latex enlarged with the polymer particle diameter control agent exhibiting the synergistic effect of improving both impact strength and fluidity.
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The invention claimed is: 1 . A method of preparing a graft copolymer, the method comprising: adding a polymer particle diameter control agent to a conjugated diene rubber latex to prepare an enlarged conjugated diene rubber latex; and graft-polymerizing the enlarged conjugated diene rubber latex with an aromatic vinyl compound and a vinyl cyanide compound to prepare a vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer, wherein the polymer particle diameter control agent is a copolymer comprising: 0.1 to 10% by weight of methyl acrylate, 0.1 to 10% by weight of ethyl acrylate, 70 to 85% by weight of butyl acrylate, and 1 to 18% by weight of (meth)acrylic acid; a copolymer comprising 75 to 95% by weight of ethyl acrylate, 0.01 to 10% by weight of butyl acrylate, 0 to 10% by weight of methyl acrylate, and 1 to 18% by weight of (meth)acrylic acid; a copolymer comprising 82 to 99% by weight of methyl acrylate and 1 to 18% by weight of (meth)acrylic acid; or a copolymer comprising 0.01 to 10% by weight of methyl acrylate, 75 to 95% by weight of ethyl acrylate, 0.01 to 10% by weight of butyl acrylate, and 1 to 18% by weight of (meth)acrylic acid; the polymer particle diameter control agent has a glass transition temperature of 0.5 to 9.6° C., and a ratio (PS 1 /PS 2 ) of an average particle diameter (PS 1 ) of the polymer particle diameter control agent to an average particle diameter (PS 2 ) of the conjugated diene rubber latex is 0.88 to 1.13 wherein an impact strength of a thermoplastic resin composition measured according to ASTM D1238 using a specimen of the thermoplastic resin composition with a thickness of ¼″ is 27 kgf·cm/cm or more, and wherein the thermoplastic resin composition includes the graft copolymer. 2 . The method according to claim 1 , wherein the polymer particle diameter control agent has an average particle diameter of 500 to 2,000 Å. 3 . The method according to claim 1 , wherein the polymer particle diameter control agent has single glass transition temperature. 4 . The method according to claim 1 , wherein the polymer particle diameter control agent is added in an amount of 0.5 to 5 parts by weight based on 100 parts by weight of the conjugated diene rubber latex based on a solid. 5 . The method according to claim 1 , wherein the conjugated diene rubber latex has an average particle diameter of 500 to 1,500 Å. 6 . The method according to claim 1 , wherein, in the step of adding a polymer particle diameter control agent, the conjugated diene rubber latex is elevated to a temperature of 45 to 55° C., and then the polymer particle diameter control agent is added thereto, followed by stirring for 20 to 40 minutes. 7 . The method according to claim 1 , wherein the enlarged conjugated diene rubber latex has an average particle diameter of 2,500 to 4,500 Å. 8 . The method according to claim 1 , wherein, in the step of graft-polymerizing, 40 to 70% by weight of the enlarged conjugated diene rubber latex based on a solid is graft-polymerized with 5 to 20% by weight of the vinyl cyanide compound and 17 to 40% by weight of the aromatic vinyl compound. 9 . The method according to claim 1 , further comprising agglomerating the vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer. 10 . A method of preparing a thermoplastic resin composition, the method comprising: adding a polymer particle diameter control agent to a conjugated diene rubber latex to prepare an enlarged conjugated diene rubber latex; graft-polymerizing the enlarged conjugated diene rubber latex with an aromatic vinyl compound and a vinyl cyanide compound to prepare a vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer; and feeding the prepared vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer and an aromatic vinyl compound-vinyl cyanide compound copolymer into an extruder and melt-kneading the same, followed by extrusion, wherein the polymer particle diameter control agent is a copolymer comprising: 0.1 to 10% by weight of methyl acrylate, 0.1 to 10% by weight of ethyl acrylate, 70 to 85% by weight of butyl acrylate, and 1 to 18% by weight of (meth)acrylic acid; a copolymer comprising 75 to 95% by weight of ethyl acrylate, 0.01 to 10% by weight of butyl acrylate, 0 to 10% by weight of methyl acrylate, and 1 to 18% by weight of (meth)acrylic acid; a copolymer comprising 82 to 99% by weight of methyl acrylate and 1 to 18% by weight of (meth)acrylic acid; or a copolymer comprising 0.01 to 10% by weight of methyl acrylate, 75 to 95% by weight of ethyl acrylate, 0.01 to 10% by weight of butyl acrylate, and 1 to 18% by weight of (meth)acrylic acid; the polymer particle diameter control agent has a glass transition temperature of 0.5 to 9.6° C., and a ratio (PS 1 /PS 2 ) of an average particle diameter (PS 1 ) of the polymer particle diameter control agent to an average particle diameter (PS 2 ) of the conjugated diene rubber latex is 0.88 to 1.13, and wherein an impact strength of the thermoplastic resin composition measured according to ASTM D1238 using a specimen of the thermoplastic resin composition with a thickness of ¼″ is 27 kgf·cm/cm or more.
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