KR960022730A - Continuous manufacture of high gloss and impact resistant styrene resin compositions - Google Patents

Continuous manufacture of high gloss and impact resistant styrene resin compositions Download PDF

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Publication number
KR960022730A
KR960022730A KR1019940039401A KR19940039401A KR960022730A KR 960022730 A KR960022730 A KR 960022730A KR 1019940039401 A KR1019940039401 A KR 1019940039401A KR 19940039401 A KR19940039401 A KR 19940039401A KR 960022730 A KR960022730 A KR 960022730A
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South Korea
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styrene
polybutadiene
rubber
polymer
weight
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KR1019940039401A
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Korean (ko)
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김용준
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성재갑
주식회사 Lg 화학
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Priority to KR1019940039401A priority Critical patent/KR960022730A/en
Publication of KR960022730A publication Critical patent/KR960022730A/en

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Abstract

본 발명은 성형물 외관과 내충격성이 우수한 고광택, 내충격성 스티렌계 수지 조성물의 연속적 제조 방법에 관한 것으로, (A) 폴리부타디엔 1과 폴리부타디엔 2, 스티렌-부타디엔 블록 공중합체 3으로 구성되고, 폴리부타디엔 1과 폴리부타디엔 2의 중량비가 폴리부타디엔 1/폴리부타디엔 2=95/5~45/55이며, 폴리부타디엔 1과 폴리부타디엔 2의 합과 고무상 중합체 3의 중량비가(폴리부타디엔 1+폴리부타디엔 2)/고무상 중합체 3=90/10~35/65의 비율로 비닐단량체에 용해시켜 고무용액을 제조한 후, 제1반응조에 연속적으로 공급하여 중합을 행하고, (B) 제1반응조에서 중합을 행하고 고무상 중합체를 상전이시켜 전환율이 10~40중량%이고, 0.1~0.5μ 평균 입경의 고무입자가 10~65%, 0.6~1.2μ평균입경의 고무입자가 85~15%, 1.3~4.0μ평균입경의 고무입자가 5~20%로 이루어진 3가지 입자사이즈 분포로 되는 고무입자를 생성시키고, (C) 상기 제1반응조건에서 생성된 반응액을 제2, 제3, 제4반응조에 연속적으로 공급하여 단량체의 전환율이 65~90중량%로 될 때까지 중합을 행하며, (D) 제4반응조에서의 반응액을 연속적으로 탈휘발장치로 공급하여 고무성분을 포함한 중합체와 미반응 단량체를 분리시켜서, (E) 탈휘발된 고무성분을 포함한 중합체가 고무변성 스티렌 수지 조성물의 8 중량부 이상으로서 코아셀 구조와 살라미 구조로 이루어짐을 특징으로 한다.The present invention relates to a continuous manufacturing method of a high-gloss, impact-resistant styrene resin composition excellent in molding appearance and impact resistance, comprising (A) polybutadiene 1, polybutadiene 2, styrene-butadiene block copolymer 3, polybutadiene The weight ratio of 1 to polybutadiene 2 is polybutadiene 1 / polybutadiene 2 = 95/5 to 45/55, and the sum of polybutadiene 1 and polybutadiene 2 and the weight ratio of rubbery polymer 3 (polybutadiene 1 + polybutadiene 2 ) / Rubber polymer 3 dissolved in a vinyl monomer at a ratio of 90/10 to 35/65 to prepare a rubber solution, and then continuously supplied to the first reactor to carry out polymerization, and (B) polymerization in the first reactor. The phase transition of the rubbery polymer was carried out so that the conversion was 10 to 40% by weight, 10 to 65% of the rubber particles having a mean particle size of 0.1 to 0.5 μm, 85 to 15% of the rubber particles having a mean particle size of 0.6 to 1.2 μm, and 1.3 to 4.0 μm. Three types of rubber particles with an average particle diameter of 5 to 20% Rubber particles having a size distribution are produced, and (C) the reaction solution produced under the first reaction conditions is continuously supplied to the second, third, and fourth reaction tanks so that the conversion rate of the monomer is 65 to 90% by weight. Polymerization until the reaction solution (D) is continuously supplied to the devolatilization apparatus to separate the polymer including the rubber component from the unreacted monomer, and (E) the polymer containing the devolatilized rubber component is At least 8 parts by weight of the rubber-modified styrene resin composition is characterized by consisting of a corel structure and a salami structure.

Description

고광택, 내충격성 스티렌계 수지 조성물의 연속적 제조방법Continuous manufacturing method of high gloss and impact resistant styrene resin composition

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음As this is a public information case, the full text was not included.

Claims (3)

3가지 입자사이즈 분포로 된 고무입자를 분산상으로 갖는 고광택, 내충격성, 스티렌계 수지조성물의 제조방법에 있어서, (A) 5% 스티렌 용액점도가 10~50 CPS로 된 폴리부타디엔 1과 5% 스티렌 용액점도가 70~200CPS로 된 폴리 부타디엔 2, 5% 스티렌용액점도가 10~40CPS로서 스티렌 함유량이 20~50중량부로 된 스티렌-부타디엔 블록 공중합체 3으로 구성되고, 폴리부타디엔 1과 폴리부타디엔 2의 중량비가 폴리부타디엔 1/폴리부타디엔 2=95/5~45/55이며, 폴리부타디엔 1과 폴리부타디엔 2의 합과 고무상 중합체 3의 중량비가 (폴리부타디엔 1+폴리부타디옌 2)/고무상 중합체 3=90/10~35/65의 비율로 비닐단량체에 용해시켜 고무용액을 제조한 후, 제1반응조에 연속적으로 공급하여 중합을 행하고, (B) 제1반응조에서 반응온도 120~145℃, 교반기의 교반회전수 50~500RPM인 조건하에서 중합을 행하고 고무상 중합체를 상전이시켜 단량체의 중합체로서 전환율이 10~40중량%이고, 0.1~0.5μ평균 입경의 고무입자가 10~65%, 0.6~1.2μ평균 입경의 고무입자가 85~15%, 1.3~4.3μ평균입경의 고무입자가 5~20%로 이루어진 3가지 입자사이즈 분포로 되는 고무입자를 생성시키고, (C) 상기 제1반응조건에서 생성된 반응액을 제2, 제3, 제4반응조에 연속적으로 공급하여 단량체의 전환율이 65~90중량%로 될 때까지 중합을 행하며, (D) 제4반응조에서의 반응액을 연속적으로 탈취발장치로 공급하여 고무성분을 포함한 중합체와 미반응 단량체를 분리시켜서 (E) 탄휘발된 고무성분을 포함한 중합체가 고무변성 스티렌 수지 조성물의 8중량부 이상으로서 코아셀 구조와 살라미 구조를 갖는 스티렌계 수지조성물을 제조하는 것을 특징으로 하는 고광택, 내충격성 스티렌계 수지조성물의 연속적 제조방법.(A) 5% styrene polybutadiene 1 and 5% styrene having a 5% styrene solution viscosity of 10 to 50 CPS in a method for producing a high gloss, impact resistance, and styrene resin composition having rubber particles having three particle size distributions in a dispersed phase. Polybutadiene 2 with a solution viscosity of 70 to 200 CPS, 5% styrene solution viscosity with 10 to 40 CPS, consisting of styrene-butadiene block copolymer 3 with a styrene content of 20 to 50 parts by weight, and polybutadiene 1 and polybutadiene 2 The weight ratio of polybutadiene 1 / polybutadiene 2 = 95/5 to 45/55, and the sum of polybutadiene 1 and polybutadiene 2 and the weight ratio of rubber polymer 3 (polybutadiene 1 + polybutadiene 2) / rubber polymer After dissolving in a vinyl monomer at a ratio of 3 = 90/10 to 35/65 to prepare a rubber solution, the rubber solution was continuously supplied to the first reactor to carry out polymerization, and (B) the reaction temperature was 120 to 145 ° C. in the first reactor. Under the condition that the stirring speed of the stirrer is 50 to 500 RPM By combining and phase-transferring the rubbery polymer to convert the monomer as a polymer of 10 to 40% by weight, 10 to 65% of rubber particles having a mean particle size of 0.1 to 0.5 μm, and 85 to 15 of rubber particles having a mean particle size of 0.6 to 1.2 μm. %, Rubber particles having a particle size distribution of 1.3 to 4.3 mu average particle diameter of 5 to 20% to produce a rubber particle having a three particle size distribution, (C) the reaction solution produced under the first reaction conditions, the second and third , The polymer was continuously supplied to the fourth reactor until the conversion of the monomer was 65 to 90% by weight, and (D) the polymer containing the rubber component was continuously fed to the deodorizing device from the reaction solution in the fourth reactor. And the unreacted monomer to separate (E) a high gloss, characterized in that the polymer containing the carbon component is a rubber-modified styrene resin composition to produce a styrene resin composition having a corel structure and a salami structure as at least 8 parts by weight of the rubber-modified styrene resin composition. , Impact resistance styrene Continuous preparation of paper compositions. 제1항에 있어서, 비닐단량체가 스티렌, 메틸스티렌, 에틸스티렌, 이소프로필스티렌, 부틸스티렌등의 알킬스티렌, 클로로스티렌, 브롬스티렌등의 비닐스티렌 또는 할로겐화 스티렌, 할로겐화 알킬스티렌등의 치환체 스티렌중에서 선택된 적어도 1종인 것을 특징으로 하는 고광택, 내충격성 스티렌계 수지 조성물의 연속적 제조방법 .The vinyl monomer according to claim 1, wherein the vinyl monomer is selected from styrene, methyl styrene, ethyl styrene, isopropyl styrene, alkyl styrene such as butyl styrene, vinyl styrene such as chloro styrene and bromine styrene, or substituted styrene such as halogenated styrene and halogenated alkyl styrene. A continuous production method of a high gloss and impact resistance styrene resin composition, characterized in that at least one kind. 제1항에 있어서, 고무상 중합체가 폴리부타디엔, 스티렌, 부타디엔 공중합체, 에틸렌-프로필렌계 공중합체, 에틸렌-프로필렌-터폴리머계 공중합체, 부타디엔-아크릴로니트릴 공중합체 중에서 1종 또는 2종 이상 선택되는 것을 특징으로 하는 고광택, 내충격성 스티렌계 수지 조성물의 연속적 제조방법.The rubber polymer according to claim 1, wherein the rubbery polymer is one or two or more of polybutadiene, styrene, butadiene copolymer, ethylene-propylene copolymer, ethylene-propylene-terpolymer copolymer and butadiene-acrylonitrile copolymer. A continuous manufacturing method of a high gloss and impact resistant styrene resin composition, characterized in that it is selected. ※ 참고사항 :최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019940039401A 1994-12-30 1994-12-30 Continuous manufacture of high gloss and impact resistant styrene resin compositions KR960022730A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100375817B1 (en) * 2000-12-08 2003-03-15 제일모직주식회사 Thermoplastic Resin Having High Gross and High Impact Strength Resistance and Method of Preparing the Same
KR100576325B1 (en) * 1999-12-17 2006-05-03 제일모직주식회사 Continuous Process for Preparing High Impact Polystyrene Resin
KR100583525B1 (en) * 2000-06-02 2006-05-24 제일모직주식회사 High Impact Polystyrene Resin with Good Falling Dart Impact and Anti-Abrasion Prepared by Continuous Mass Polymerization Process
KR100583524B1 (en) * 1999-12-17 2006-05-24 제일모직주식회사 High Impact Polystyrene Resin with Good Falling Dart Impact Prepared by Continuous Mass Polymerization process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100576325B1 (en) * 1999-12-17 2006-05-03 제일모직주식회사 Continuous Process for Preparing High Impact Polystyrene Resin
KR100583524B1 (en) * 1999-12-17 2006-05-24 제일모직주식회사 High Impact Polystyrene Resin with Good Falling Dart Impact Prepared by Continuous Mass Polymerization process
KR100583525B1 (en) * 2000-06-02 2006-05-24 제일모직주식회사 High Impact Polystyrene Resin with Good Falling Dart Impact and Anti-Abrasion Prepared by Continuous Mass Polymerization Process
KR100375817B1 (en) * 2000-12-08 2003-03-15 제일모직주식회사 Thermoplastic Resin Having High Gross and High Impact Strength Resistance and Method of Preparing the Same

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