Method of preparing graft copolymer and method of preparing thermoplastic resin composition including the same

US12492277B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12492277-B2
Application numberUS-202117771679-A
CountryUS
Kind codeB2
Filing dateJul 22, 2021
Priority dateSep 18, 2020
Publication dateDec 9, 2025
Grant dateDec 9, 2025

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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Abstract

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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.

First claim

Opening claim text (preview).

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.

Assignees

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Classifications

  • Methyl esters {, e.g. methyl (meth)acrylate} · CPC title

  • Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof · CPC title

  • C08F6/18Primary

    Increasing the size of the dispersed particles · CPC title

  • C2-(meth)acrylate, e.g. ethyl (meth)acrylate · CPC title

  • C4-(meth)acrylate, e.g. butyl (meth)acrylate, isobutyl (meth)acrylate or tert-butyl (meth)acrylate · CPC title

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What does patent US12492277B2 cover?
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 tha…
Who is the assignee on this patent?
Lg Chemical Ltd
What technology area does this patent fall under?
Primary CPC classification C08F6/18. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Dec 09 2025 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 5 related publications on this page (citations in our corpus or others sharing the same primary CPC).