KR890003537B1 - The method of polymerization thermerplastic in suspension pr massive by mma acrylonitril and stylene - Google Patents

The method of polymerization thermerplastic in suspension pr massive by mma acrylonitril and stylene Download PDF

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KR890003537B1
KR890003537B1 KR1019860001161A KR860001161A KR890003537B1 KR 890003537 B1 KR890003537 B1 KR 890003537B1 KR 1019860001161 A KR1019860001161 A KR 1019860001161A KR 860001161 A KR860001161 A KR 860001161A KR 890003537 B1 KR890003537 B1 KR 890003537B1
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polymerization
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와이.리 토마스
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신아화학공업 주식회사
이원용
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/18Suspension polymerisation
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/02Polymerisation in bulk

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Abstract

A thermoplastic resin having an excellent transparency, high surface hardness and weatherability is prepd. by the suspension polymn. of 5- 35 wt.% MMA, 45-80 wt.% styrene and 5-35 wt.% acrylonitrile. The suspension polymn. of the three monomers is carried out by reacting in a mixed soln. of pure water and cellosize at 70-115≰C for 8 hrs, and by adding an antioxidant.

Description

MMA, 아크릴로 니트릴 및 스티렌에 의한 현탁 및 괴상현탁중합으로 열가소성 수지를 제조하는 방법Process for preparing thermoplastic resins by suspension and bulk suspension polymerization by MMA, acrylonitrile and styrene

본 발명은 엠엠에이, 아클릴로니트릴 및 스티렌의 3성분으로 현탁중합 또는 과상현탁중합을 시켜 높은 수율을 갖는 열가소성 수지를 제조하는 방법에 관한 것이다.The present invention relates to a method for producing a thermoplastic resin having high yield by suspension polymerization or superphase suspension polymerization with three components of MMA, acrylonitrile and styrene.

미국특허 4056671 및 일본특허 49-37836등에 의하면 스티렌, 아크릴로니트릴의 공중합체인 SAN 수지 및 스티렌, 엠엠에이 공중합체인 MS 수지가 나와 있다.U.S. Patent 4056671 and Japanese Patent No. 49-37836 and the like disclose SAN resin which is a copolymer of styrene and acrylonitrile and MS resin which is a styrene and MMA copolymer.

SAN 수지는 열안정성 및 표면경도가 약하고, MS 수지는 내약품성의 결점을 갖는다.SAN resins have poor thermal stability and surface hardness, and MS resins have drawbacks of chemical resistance.

일본 공개특허 58-217544에 의하면 아크릴로니트릴, 엠엠에이의 공중합체와 스티렌, 아크릴로니트릴의 공중합체를 용융온도까지 올린 후 혼합하는 방법이 있지만, 이는 물성의 균일화를 갖기 어렵다. 한국특허 출원번호 80-1645에 의하면, α-메틸스티렌, 엠엠에이 및 아크릴로니트릴을 유화중합에 의하면 중합된 열가소성 수지가 나와있다.According to Japanese Patent Application Laid-Open No. 58-217544, there is a method of raising a copolymer of acrylonitrile and MMA with a copolymer of styrene and acrylonitrile to a melting temperature and then mixing them, but it is difficult to have uniformity of physical properties. According to Korean Patent Application No. 80-1645, a thermoplastic resin polymerized by emulsion polymerization of α-methylstyrene, MMA and acrylonitrile is shown.

본 발명에서는 α-메틸스티렌 대신 스티렌을 사용하였고 중합방법을 현탁중합, 또는 과상현탁중합 방법을 행하였다. 엠엠에이계의 중합체는 광학적 특성, 내후성이 높은 표면강도를 가지며, 흡수성이 크로 내약품성의 약점을 갖는다.In the present invention, styrene was used instead of α-methylstyrene, and the polymerization method was subjected to suspension polymerization or superphase suspension polymerization. MMC polymers have high optical properties, weather resistance and high surface strength, and absorbability has a weak chemical resistance.

그리고 아크릴로니트릴, 스티렌의 공중합체는 투명하며 내약품성이 우수하고 경제성이 있지만 때로는 우수한 투명도, 표면경도, 내후성을 요구하는 경우가 있으므로 엠엠에이, 아크릴로니트릴, 스티렌의 3성분을 중합함으로써 결점을 개량하기 위하여 본 발명을 개발 하였다.Copolymers of acrylonitrile and styrene are transparent, have excellent chemical resistance and economical efficiency, but sometimes they require excellent transparency, surface hardness, and weather resistance. Thus, polymerizing three components of MMA, acrylonitrile, and styrene may be used. The present invention was developed to improve.

본 발명에서 3성분의 중합영향을 보면 스티렌을 많이 첨가될수록 중합속도는 늦어지나 성형품의 치수안정성이 우수하며, 중량으로 45-80% 범위이다. 아크릴로니트릴은 그량이 증가할수록 중합속도는 빨라지고 치수안정성은 떨어지며, 내열성은 증가된다. 따라서 물성의 균형을 유지하기 위하여 5-35% 범위이다. 메틸메타크릴레이트는 량이 증가할수록 중합속도는 빨라지고 중합반응계는 불안정하게 된다. 따라서 5-35% 범위이다. 이 수지는 ABS와 혼합이 가능하며, 단독으로 사용될 때는 투명제품으로써 내약품성, 내후성 및 고인장성을 요구하는 성형품에 사용되어진다. 중합촉매로서는 저온촉매와 고온촉매를 조합시키어 사용하였다.In view of the polymerization effect of the three components in the present invention, the more the styrene is added, the slower the polymerization rate, but the dimensional stability of the molded article is excellent, and the weight ranges from 45 to 80%. As the amount of acrylonitrile increases, the polymerization rate increases, the dimensional stability decreases, and the heat resistance increases. Therefore, in order to maintain the balance of physical properties, the range is 5-35%. As the amount of methyl methacrylate increases, the polymerization rate becomes faster and the polymerization system becomes unstable. Therefore, it is in the range of 5-35%. This resin can be mixed with ABS, and when used alone, it is a transparent product and is used in molded articles requiring chemical resistance, weather resistance and high tensile resistance. As the polymerization catalyst, a low temperature catalyst and a high temperature catalyst were used in combination.

[표 1]TABLE 1

현 탁 중 합 (숫치는 Wt%)Suspension Polymerization (Value Wt%)

Figure kpo00001
Figure kpo00001

표 1)의 중합반응 방법은 먼저 순수와 셀로사이즈를 혼합하고 60℃에서 20분동안 용해시킨다. 나머지 모든 처리화합물을 첨가하고 질소로 반응조에 들어 있는 공기를 추출하고 압력을 채워서 공기가 투입되지 못하도록 하면서 70-75℃에서 2시간, 80-85℃에서 3시간, 115℃에서 3시간동안 중합반응을 한후 90℃로 온도를 내린 후 산화방지제를 첨가하고 종결한다. 중합율이 99.9%의 수지를 얻을수가 있다.In the polymerization method of Table 1), pure water and cellosize were first mixed and dissolved at 60 ° C. for 20 minutes. Add all remaining treatment compounds and extract the air in the reactor with nitrogen and fill the pressure to prevent air from being introduced. 2 hours at 70-75 ℃, 3 hours at 80-85 ℃, 3 hours at 115 ℃ After the temperature was lowered to 90 ° C., an antioxidant was added and terminated. Resin whose polymerization rate is 99.9% can be obtained.

표 1)에서 반응속도는 스티렌보다 AN, 엠엠에이 량이 증가시 빨라지며, 촉매의 량을 늘려주면 수지의 특성중 유동성은 증가되고, 저분자량이 되며, 물성은 저하하고 색상이 좋지않다. 또한 반응억지제인 메르캡탄을 늘려주면 유동성은 증가되나 반응속도가 느려지고 미반응된 물질이 많기 때문에 적당량을 찾아서 사용한다.In Table 1, the reaction rate is faster when the amount of AN and M is increased than styrene, and increasing the amount of catalyst increases the fluidity of the resin, lower molecular weight, lowers the physical properties, and the color is not good. In addition, increasing the reaction inhibitor mercaptan increases the fluidity, but the reaction rate is slowed down and many unreacted substances are used to find an appropriate amount.

[표 2]TABLE 2

괴 상 현 탁 중 합Lump suspension polymerization

Figure kpo00002
Figure kpo00002

표 2)에서 과상중합은 전체의 처리화합물을 반응기에 넣고, 질소 개스로 공기를 추출하며, 공기가 들어오지 못하도록 압력을 채워준 후, 75℃에서 1시간, 80-85℃에서 4시간 중합을 시키면 표 3)과 같은 특성을 얻는다.In Table 2), the superphase polymerization is carried out by putting the whole treated compound into a reactor, extracting air with nitrogen gas, filling the pressure to prevent air from entering, and then performing polymerization at 75 ° C. for 1 hour and at 80-85 ° C. for 4 hours. Obtain the same characteristics as 3).

[표 3]TABLE 3

중합시간에 따른 점도 및 고체함량Viscosity and Solid Content According to Polymerization Time

Figure kpo00003
Figure kpo00003

표 3)에서와 같이 점도가 6000-8000CP, 고체함량이 40-45%되었을때 중합을 중지하고 현탁중합반응조로 옮긴다. 현탁중합반응조에서 질소 개스로 공기를 추출후 70-75℃에서 2시간, 80-85℃에서 3시간 30분, 115℃에서 3시간 중합을 한 후 반응을 종결한다. 90℃로 온도를 내린 후 산화방지제를 첨가한다.As shown in Table 3), when the viscosity is 6000-8000CP and the solid content is 40-45%, the polymerization is stopped and transferred to the suspension polymerization reactor. After extracting air with nitrogen gas from the suspension polymerization reactor, polymerization is completed for 2 hours at 70-75 ° C, 3 hours 30 minutes at 80-85 ° C, and 3 hours at 115 ° C. Lower the temperature to 90 ° C. and add antioxidant.

괴상현탁중하 방법에서도 단량체가 중합에 주는 영향을 보면 현탁중합에서 나타낸 바와 같으며, 현탁중합에서는 발영이 심하여 분자량 조절이 힘드나, 낮은 온도에서 40-45% 괴상중합을 한후 현탁중합 방법으로 반응을 하기 때문에 물성의 균일화를 가질수가 있다.The effect of the monomer on the polymerization in the bulk suspension method is as shown in the suspension polymerization, and in suspension polymerization, it is difficult to control the molecular weight due to the high expression in the suspension polymerization, but the reaction is carried out by the suspension polymerization method after the 40-45% block polymerization at low temperature. Therefore, the physical properties can be uniform.

[표 4]TABLE 4

물 성 비 교 표Property comparison table

Figure kpo00004
Figure kpo00004

주석 : SAN : Styrene acryonitrileTin: SAN: Styrene acryonitrile

MS : Methylmetacrylate styerneMS: Methylmetacrylate styerne

AN : Acrylonitryl(아크릴로니트릴)AN: Acrylonitryl

MMA : 메틸메타크릴레이트MMA: Methyl methacrylate

표 4)의 물성시험 방법은 아이조드 충격강도(ASTD D-256), 인장강도(SATM D-638), 신율(ASTM D-638), 굴곡강도(ASTM D-790), 유동성(ASTM D-1238), 경도(ASTM D-785)로 하였음.Physical property test method of table 4) iszod impact strength (ASTD D-256), tensile strength (SATM D-638), elongation (ASTM D-638), flexural strength (ASTM D-790), fluidity (ASTM D-1238) ) And hardness (ASTM D-785).

이 수지는 에이비에스 수지와 혼합 사용 가능하며, 자체로서는 우수한 투명도, 표면강도, 인장강성 및 내약품성 특징을 가지므로 일반 사출성형품에 적용된다.This resin can be mixed with ABS resin, and because it has excellent transparency, surface strength, tensile strength and chemical resistance, it is applied to general injection molded products.

본 발명에 의한 수지는 표면 경도가 높고, 내후성, 내약품성의 특징이 있고, 다른 수지와의 상용성이 양호하다.The resin according to the present invention has high surface hardness, features weather resistance and chemical resistance, and has good compatibility with other resins.

Claims (3)

MMA(Methylmethacylate), 스티렌(Styrene) 및 아크릴로니트릴(Acrylonitle)을 사용하며, 현탁중합 및 괴상현탁중합을 시켜 높은 수율의 열 가소성 합성수지를 제조하는 방법에 있어서, 상기 현탁중합과 괴상 중합을 할때 모노머(Monomer)로서 스티렌 45-80Wt%, 아크릴로니트릴 5-35Wt%, MMA 5-35Wt%의 범위로 처리 시킴을 특징으로 한 상기 방법.MMA (Methylmethacylate), styrene (Styrene) and acrylonitrile (Acrylonitle), and a method of producing a high yield of thermoplastic synthetic resin by suspension polymerization and bulk suspension polymerization, when the suspension polymerization and bulk polymerization The above method, characterized in that the monomer is treated in the range of 45-80 Wt% of styrene, 5-35 Wt% of acrylonitrile, and 5-35 Wt% of MMA. 제1항에 있어서, 상기 현탁중합은 순수한물(pure water)과 셀로사이즈(Cellosize)를 혼합시켜 용해시킨 다음 스티렌, 아크릴레이트, MMA 등의 처리 화합물을 반응조에 첨가시키고, 중합반응을 시킨후 (70-75℃ 2시간, 80-85℃ 3시간, 115℃ 3시간) 온도를 저하시켜 산화방지제의 첨가로 중합반응을 종결시킴을 특징으로 한 상기 방법.The method of claim 1, wherein the suspension polymerization is dissolved by mixing pure water and cellosize (Cellosize), and then adding a treating compound such as styrene, acrylate, MMA to the reaction tank, and performing a polymerization reaction ( 70-75 ° C., 2 hours, 80-85 ° C., 3 hours, 115 ° C., 3 hours) by lowering the temperature to terminate the polymerization reaction by adding an antioxidant. 제1항에 있어서, 상기 괴상현탁중합은 처리 화합물 전체를 반응기에 넣고 질소 가스로 공기를 추출시켜 압력을 유지시킨다음 중합시켜(75℃ 1시간, 80-85℃ 4시간) 점도 6000-8000Cp 고체함량 40-45 Wt% 일때, 중합을 중지하고, 현탁중합반응조에서 중합시켜 (70-75℃ 2시간, 80-85℃ 3시간 30분, 115℃ 3시간)반응을 종결시킴을 특징으로 한 상기 방법.The method of claim 1, wherein the bulk suspension polymerization is carried out by placing the entire processing compound into the reactor to extract the air with nitrogen gas to maintain the pressure and then polymerized (75 ℃ 1 hour, 80-85 ℃ 4 hours) viscosity 6000-8000Cp solid When the content is 40-45 Wt%, the polymerization is stopped and polymerized in a suspension polymerization reactor (70-75 ° C 2 hours, 80-85 ° C 3 hours 30 minutes, 115 ° C 3 hours) to terminate the reaction. Way.
KR1019860001161A 1986-02-19 1986-02-19 The method of polymerization thermerplastic in suspension pr massive by mma acrylonitril and stylene KR890003537B1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100690344B1 (en) * 2004-12-11 2007-03-09 주식회사 엘지화학 Method for producing transparent copolymer resin having good chemical resistance, fluidity and fading resistance, and copolymer resin prepared by the method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100690344B1 (en) * 2004-12-11 2007-03-09 주식회사 엘지화학 Method for producing transparent copolymer resin having good chemical resistance, fluidity and fading resistance, and copolymer resin prepared by the method

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