WO2015047038A1 - Abs 그라프트 공중합체의 제조방법 - Google Patents
Abs 그라프트 공중합체의 제조방법 Download PDFInfo
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- WO2015047038A1 WO2015047038A1 PCT/KR2014/009220 KR2014009220W WO2015047038A1 WO 2015047038 A1 WO2015047038 A1 WO 2015047038A1 KR 2014009220 W KR2014009220 W KR 2014009220W WO 2015047038 A1 WO2015047038 A1 WO 2015047038A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/12—Polymerisation in non-solvents
- C08F2/16—Aqueous medium
- C08F2/22—Emulsion polymerisation
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F279/00—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00
- C08F279/02—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00 on to polymers of conjugated dienes
- C08F279/04—Vinyl aromatic monomers and nitriles as the only monomers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L55/00—Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
- C08L55/02—ABS [Acrylonitrile-Butadiene-Styrene] polymers
Definitions
- the present invention relates to a method for producing an ABS graft copolymer, and more particularly, to induce bimodal particle formation by formation of ABS resin particles having a relatively small particle size with existing ABS resin particles, thereby improving surface glossiness. It relates to a method for producing an ABS graft copolymer that can be improved.
- ABS graft copolymers are prepared by emulsion polymerization, obtained by polybutadiene latex (PBL) as a seed, and graft copolymerization of SAN to the seed.
- PBL polybutadiene latex
- ABS resin acrylonitrile-butadiene-styrene resin
- surface glossiness improvement is a potential property of consumers. It was. This is because, in general, people perceive high-gloss products as high-end products in televisions, refrigerators and automobiles.
- the improvement of glossiness is also an important task in order to differentiate the quality of the ABS resin that is already generalized from the quality of the ABS resin of other companies.
- an object of the present invention is to provide a method for producing an ABS graft copolymer with improved gloss and an ABS graft copolymer prepared therefrom.
- the method for preparing the ABS graft copolymer according to the present invention comprises graft copolymerization of a vinyl aromatic monomer and a vinyl cyan monomer to rubber latex to produce an ABS graft copolymer, wherein the rubber latex, the vinyl aromatic monomer and the vinyl cyan
- the total of rubber latex, vinylaromatic monomer and vinylcyan monomer Based on the weight of 100 parts by weight (1) 50 to 80% by weight of the rubber latex (based on solids) 0.0001 to 0.1 parts by weight of an aqueous polymerization initiator, and mixing to obtain a first mixture;
- Initiating polymerization by incorporating 5 to 10% by weight of the monomer emulsion mixture in which 20 to 50% by weight of the second mixture of the vinylaromatic monomer and the vinyl cyan monomer
- the first polymerization step of polymerization by continuously adding the residual monomer emulsion mixture; And (3) a secondary polymerization step of adding and polymerizing 0.0001 to 0.5 parts by weight of an auxiliary polymerization initiator at a polymerization conversion rate of 80 to 90% during the progress of the polymerization step.
- the method of preparing the ABS graft copolymer that is, the amount of water used in the polymerization may be, for example, 90 to 200 parts by weight, 90 to 150 parts by weight, or 90 to 120 parts by weight based on 100 parts by weight of the total rubber and monomer.
- Water used in the polymerization may be used, for example, 70 to 95% by weight, or 80 to 90% by weight in the preparation of the first mixture, the rest may be used in the preparation of the monomer emulsion mixture.
- a small particle size graft is obtained by separately using a polymerization initiator and partially adding an emulsion mixture of a vinyl aromatic monomer and a vinyl cyan monomer which are graft-polymerized to rubber latex, and the other is continuously added. Forming a large amount of the copolymer has the effect of providing an ABS graft copolymer with improved surface gloss.
- Example 1 is a transmission electron microscope (TEM) photograph of an ABS graft copolymer obtained according to Example 1 of the present invention.
- Example 2 is a transmission electron micrograph of the ABS graft copolymer obtained according to Example 2 of the present invention.
- Example 3 is a transmission electron micrograph of the ABS graft copolymer obtained according to Example 3 of the present invention.
- the ABS graft copolymer refers to a copolymer obtained by graft polymerization of a vinyl aromatic monomer and a vinyl cyan monomer on a diene rubber, and may be represented as an acrylonitrile-butadiene-styrene-based graft copolymer. .
- the method for preparing the ABS graft copolymer according to the present invention comprises graft copolymerization of a vinyl aromatic monomer and a vinyl cyan monomer to rubber latex to produce an ABS graft copolymer, wherein the rubber latex, the vinyl aromatic monomer and the vinyl cyan
- the total of rubber latex, vinylaromatic monomer and vinylcyan monomer Based on the weight of 100 parts by weight (1) 50 to 80% by weight of the rubber latex (based on solids) 0.0001 to 0.1 parts by weight of an aqueous polymerization initiator, and mixing to obtain a first mixture; (2) 5 to 10% by weight of the monomer emulsion mixture in which 20 to 50% by weight of the second mixture of the vinylaromatic monomer and the vinyl cyan monomer was emulsified with 0.01 to
- the first polymerization step of polymerization by adding the residual monomer emulsion mixture and (3) a secondary polymerization step of adding and polymerizing 0.0001 to 0.5 parts by weight of an auxiliary polymerization initiator at a polymerization conversion rate of 80 to 90% during the progress of the polymerization step.
- 5 to 10% by weight of the emulsified monomer emulsion mixture may be a batch injection as an example.
- the first polymerization step for example, 5 to 10% by weight of the monomer emulsion mixture is added, and then the temperature of the reactor is increased to 70 to 80 ° C. to initiate polymerization.
- the input of the residual monomer emulsion mixture may be, for example, a continuous input.
- the continuous addition of the residual monomer emulsion mixture starts at the time when the polymer particle content calculated using the polymerization conversion rate is 5 to 10% by weight. This is because the monomers that are added in batches react for a certain time to make more reaction sites in addition to the conventional rubber latex, and the monomers are continuously added after the point where the polymer particle content calculated using the polymerization conversion rate is 5 to 10% by weight. There is an effect that more particles are formed by these, thereby improving the gloss.
- Continuous addition of the residual monomer emulsion mixture may be carried out, for example, until the polymerization conversion rate reaches 80 to 90%.
- the continuous dosing method is, for example, continuous dosing of the residual monomer emulsion mixture continuously for at least 60 minutes and 60 to 120 minutes.
- the continuous dosing method is to start the residual monomer emulsion mixture at 5 to 10% polymerization conversion rate and then continuously add at least 60 minutes, 60 minutes to 120 minutes, or at least 60% polymerization conversion rate. .
- the aqueous polymerization initiator is not particularly limited when the initiator can be used in the preparation of the graft copolymer of the present invention, preferably or may be potassium persulfate, sodium persulfate, ammonium persulfate or butyl hydroperoxide and the like. have.
- the aqueous polymerization initiator is 0.0001 to 0.1 parts by weight, 0.001 to 0.09 parts by weight, 0.01 to 0.05 parts by weight, or 0.018 to 0.036 based on 100 parts by weight of the total weight of the rubber latex, the vinylaromatic monomer and the vinyl cyan monomer. Add weight parts. If the content of the aqueous polymerization initiator is less than 0.0001 parts by weight, the radicals are not sufficiently generated for the reaction to be initiated. If the amount of the aqueous polymerization initiator exceeds 0.1 parts by weight, a large amount of radicals are generated, and thus the reaction is easily terminated.
- an auxiliary polymerization initiator is added at 0.0001 to 0.5 parts by weight, 0.001 to 0.4 parts by weight, 0.01 to 0.3 parts by weight, or 0.05 to 0.2 parts by weight at 80 to 90% of the polymerization conversion rate. If the auxiliary polymerization initiator content is less than 0.001 parts by weight, the radicals for initiating the reaction may not be sufficiently generated. If the auxiliary polymerization initiator is more than 0.5 parts by weight, a large amount of radicals may be generated, and thus the reaction may be easily terminated.
- the auxiliary polymerization initiator is an initiator having low solubility in water as compared with the aqueous initiator introduced at the start of the graft polymerization, and in this case, the gloss, impact strength, and graft efficiency are excellent.
- the auxiliary polymerization initiator may include, for example, peroxides such as cumene hydroperoxide, diisopropyl benzene hydroperoxide, persulfate, and the like;
- peroxides such as cumene hydroperoxide, diisopropyl benzene hydroperoxide, persulfate, and the like
- redox-based catalyst made of a mixture with a reducing agent such as sodium formaldehyde siloxylate, sodium ethylenediamine tetraacetate, ferrous sulfate, dextrose, sodium pyrroline, sodium sulfite and the like It can be abnormal.
- the molecular weight modifier may be further included, for example, 0.0001 to 0.3 parts by weight, 0.0001 to 0.2 parts by weight, 0.0001 to 0.1 parts by weight, or 0.0001 to 0.01 parts by weight. If the molecular weight modifier is less than 0.0001 parts by weight or more than 0.3 parts by weight, there is a problem that the weight average molecular weight is larger or smaller than 50,000 to 100,000 g / mol which is the weight average molecular weight required in the final ABS product.
- the molecular weight modifier may preferably be mercaptans, more preferably tertiary dodecyl mercaptan or n-octyl mercaptan, most preferably tertiary dodecyl mercaptan.
- the emulsifier may be appropriately selected from those used in the graft copolymer, and the content thereof is, for example, 0.01 to 10 parts by weight, 0.1 to 5 parts by weight, or 0.2 to 2 parts by weight. If the emulsifier content is less than 0.01 parts by weight, it is insufficient to stabilize the surface area increased by the formation of small particles, and if more than 10 parts by weight, the surface sharpness due to the emulsifier is deteriorated.
- the rubber latex may have a mean particle size of at least 1500 kPa, preferably from 1500 to 5000 kPa, more preferably from 2500 to 5000 kPa of large diameter rubber latex.
- the average particle diameter may be measured using a particle size analyzer (NICOMP 380).
- the rubber latex is 50 to 80% by weight (based on solids), 55 to 75% by weight, or 60 to 70% by weight based on a total of 100% by weight of the rubber latex, aromatic vinyl compound and vinyl cyan compound in total.
- the rubber latex at this time may have a gel content of 50 to 95%, preferably 55 to 90%.
- Styrene, ⁇ -methylstyrene, o-ethylstyrene, p-ethylstyrene and vinyltoluene may be used as the vinylaromatic monomer, and the content thereof is 100% by weight in total of rubber latex, aromatic vinyl compound, and vinyl cyan compound.
- the amount may be in the range of 0.1 to 49.9% by weight, 10 to 40% by weight, or 10 to 30% by weight.
- the vinyl cyan compound for example, acrylonitrile or methacrylonitrile may be used, and the content thereof is, for example, 0.1 to 49.9 weight based on a total of 100 weight% of the rubber latex, the aromatic vinyl compound, and the vinyl cyan compound. %, 1 to 30% by weight, or 1 to 20% by weight.
- the graft ratio of the graft polymerization is, for example, within the range of 25 to 40%, 27 to 35%, or 28 to 32%. Within this range, flowability and glossiness are excellent.
- the polymerization conversion rate is, for example, at least 94%, preferably at least 96%, more preferably at least 98%.
- the ABS graft copolymer obtained according to the present invention has a weight average molecular weight of, for example, within the range of 50,000 to 100,000 g / mol, 65,000 to 85,000 g / mol, 70,000 to 80,000 g / mol, or 70,000 to 79,000 g / mol. Can be.
- the polymerization temperature is 45 to 80 ° C. and the polymerization time is 3 to 6 hours in a nitrogen-substituted polymerization reactor.
- the ABS graft copolymer may be prepared by the method of manufacturing the ABS graft copolymer according to the present invention.
- the ABS graft copolymer has a gloss of 91 or more.
- the graft copolymer according to the present invention is ABS (acrylornitrile butadiene-styrene) resin as a specific example.
- the content indication of the components used in the reaction is expressed in weight percent of the rubber latex, vinylaromatic monomer and vinylcyan monomer, and components other than the monomer indicate the total weight of the rubber latex, the vinylaromatic monomer and the vinylcyan monomer. It is expressed in parts by weight based on 100 parts by weight.
- the temperature of the reactor was raised to 72 ° C. to initiate polymerization, and 30% by weight of the residual monomer emulsion mixture from the time when the amount of the polymer particles calculated using the polymerization conversion rate reached 5% by weight reached the polymerization conversion rate of 85%. It was added continuously.
- the residual monomer emulsion mixture was put in a syringe tube, and the emulsion mixture was continuously added using a syringe pump.
- 0.12 parts by weight of cumene hydroperoxide was added as an auxiliary polymerization initiator, and secondary polymerization was performed.
- the polymerization conversion reached 95%, the polymerization was terminated to prepare an ABS graft copolymer.
- Impact modifiers, antioxidants and other additives were added to the ABS graft copolymer in amounts conventionally used in the art, and then mixed and processed (extrusion and injection) to prepare specimens for measurement of physical properties.
- Example 1 10% by weight of the 35% by weight of the monomer emulsion mixture was added in the first polymerization step, and the remaining monomer emulsion mixture 25% was the time when the polymer particle amount calculated using the polymerization conversion rate was 10% by weight. The same procedure as in Example 1 was conducted except that the injection was started.
- Example 2 Except that the amount of the emulsifier was used in 1 part by weight instead of 0.5 parts by weight of 35% by weight of the second mixture of the vinylaromatic monomer and vinyl cyan monomer in Example 2 was the same as in Example 2.
- Example 1 35 wt% of the monomer emulsion mixture was added to the first mixture, followed by the same procedure as in Example 1 except that the first polymerization reaction was performed.
- Graft Efficiency (%) (weight of resin grafted to rubber / weight of rubber) x 100
- Polymerization conversion rate The polymerization liquid was collected from the reactor, and three times the amount of methanol was added to precipitate the graft copolymer resin, followed by vacuum drying to measure the final weight to measure the polymerization conversion rate. At this time, the content of unreacted monomer was measured using gas chromatography (GC) to correct the polymerization conversion measured by the precipitation method.
- GC gas chromatography
- the particle size was measured with a particle size analyzer (NICOMP 380), and the solid content at the time of sampling was calculated by the following equation.
- Solids content number of particles * volume of one particle * density
- Example 1 compared to Comparative Example 1 in which all of the emulsified monomer emulsion mixture is added in batch, Example 1 in which some of the monomer emulsion mixture is added in batch and the remainder is continuously added, the number of particles is significantly increased. As a result, it was confirmed that not only the polymerization conversion rate was improved but also the gloss was also increased.
- Example 2 which increased the amount of the monomer emulsion mixture added in a batch and reduced the amount of the monomer emulsion mixture added continuously, not only increased the number of particles compared to Example 1, but also increased the polymerization conversion rate and gloss. All degrees increased.
- Example 3 This increasing tendency was also well seen in Example 3, where the amount of emulsifier was increased than in Example 2. This resulted in the formation of small SAN particles with an emulsifier, which increased the polymerization conversion rate and increased the gloss. This can be seen in the transmission electron micrographs of FIGS. 1 to 4, but it was confirmed that many small particles were formed in FIGS.
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Abstract
Description
구분 | 실시예1 | 실시예 2 | 실시예 3 | 비교예 1 |
중합전환율(%) (반응시간 90분에서) | 90.5 | 91.0 | 95.0 | 90.0 |
입자 개수 | 6.23*1014 | 1.75*1015 | 8.81*1015 | 4.54*1014 |
표면광택도(gloss) | 91 | 94 | 100 | 90 |
그라프트 효율(%) | 34.0 | 39.3 | 35.0 | 32.0 |
응집율(%) | 0.04 | 0.03 | 0.09 | 0.04 |
Claims (16)
- 고무 라텍스에 비닐방향족 단량체와 비닐시안 단량체를 그라프트 공중합시켜 ABS 그라프트 공중합체를 제조함에 있어서, 상기 고무 라텍스, 상기 비닐방향족 단량체 및 상기 비닐시안 단량체의 총 중량을 100중량부로 기준하여 (1) 상기 고무 라텍스 50 내지 80중량%(고형분 기준)에 수성 중합개시제 0.0001 내지 0.1중량부를 투입하고, 혼합하여 제1 혼합물을 수득하는 혼합단계;(2) 상기 제1 혼합물에 상기 비닐방향족 단량체와 비닐시안 단량체의 제 2 혼합물 20 내지 50중량%를 유화제 0.01 내지 10중량부로 유화시킨 단량체 유화혼합물 중 5 내지 10중량%를 투입하여 중합을 개시한 후에, 잔여 단량체 유화혼합물을 투입하여 중합시키는 1차 중합단계; 및(3) 상기 중합단계의 진행 중에, 중합전환율 80 내지 90%에서 보조 중합개시제 0.0001 내지 0.5중량부를 투입하고 중합시키는 2차 중합단계;를 포함함을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 유화시킨 단량체 유화혼합물 중 5 내지 10중량%의 투입은 일괄 투입하는 것을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 잔여 단량체 유화혼합물의 투입시점은 중합전환율으로 계산한 고분자 입자의 함량이 5 내지 10중량%로 형성될 때 투입하는 것을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 잔여 단량체 유화혼합물의 투입은 연속식으로 투입하는 것을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 4 항에 있어서,상기 연속식으로 투입은 잔여 단량체 유화혼합물을 중합전환율으로 계산한 고분자 입자의 함량이 5 내지 10중량%로 형성될 때 투입을 시작하여 최소한 60분 동안 연속적으로 투입하는 것을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 수성 중합개시제가 포타슘퍼설페이트, 소듐퍼설페이트, 암모늄퍼설페이트, 부틸하이드로퍼옥사이드로 이루어지는 군으로부터 선택되는 1종 이상임을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 보조 중합개시제가 큐멘하이드로퍼옥사이드, 디이소프로필 벤젠하이드로퍼옥사이드, 과황산염; 소디움포름알데히드실폭실레이트, 소디움에틸렌디아민 테트라아세테이트, 황산 제1철, 덱스트로즈, 피롤린나트륨, 아황산 나트륨;으로 이루어지는 군으로부터 선택되는 1종 이상임을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 혼합단계 또는 상기 1차 중합단계에서 분자량 조절제가 0.0001 내지 0.3중량부로 더 포함됨을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 8 항에 있어서,상기 분자량 조절제가 3급 도데실머캅탄 또는 n-옥틸머캅탄 또는 이들의 혼합물임을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 고무 라텍스는 평균입경이 1500 내지 5000Å 인것을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 비닐방향족 단량체가 스티렌, α-메틸스티렌, o-에틸스티렌, p-에틸스티렌 및 비닐톨루엔으로 이루어지는 군으로부터 선택되는 1종 이상임을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1 항에 있어서,상기 비닐시안 화합물이 아크릴로니트릴, 메타크릴로니트릴 또는 이들의 혼합물임을 특징으로 하는 ABS 그라프트 공중합체의 제조방법.
- 제 1항 내지 제 12항 중 어느 한 항에 따른 ABS 그라프트 공중합체의 제조방법으로 제조된 ABS 그라프트 공중합체.
- 제 13 항에 있어서,상기 ABS 그라프트 공중합체는 그라프트 비율이 25 내지 40%인 것을 특징으로 하는 ABS 그라프트 공중합체.
- 제 13 항에 있어서,상기 ABS 그라프트 공중합체는 중량평균분자량이 50,000 내지 100,000g/mol인 것을 특징으로 하는 ABS 그라프트 공중합체.
- 제 13항에 있어서,상기 ABS 그라프트 공중합체는 광택(gloss)이 91 이상인 것을 특징으로 하는 ABS 그라프트 공중합체.
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US14/772,071 US9790310B2 (en) | 2013-09-30 | 2014-09-30 | Method for preparing ABS graft copolymer |
CN201480011606.3A CN105189588B (zh) | 2013-09-30 | 2014-09-30 | 一种制备abs接枝共聚物的方法 |
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KR10-2013-0116330 | 2013-09-30 | ||
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KR1020140130678A KR101582422B1 (ko) | 2013-09-30 | 2014-09-30 | Abs 그라프트 공중합체의 제조방법 |
KR10-2014-0130678 | 2014-09-30 |
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Citations (5)
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EP0003957B1 (en) * | 1978-03-03 | 1982-09-29 | Isr Holding S.A.R.L. | Process for reducing the residual styrene level of a polystyrene latex |
US4703090A (en) * | 1984-12-18 | 1987-10-27 | Enichem Polimeri S.P.A. | Method for the preparation of graft copolymers by emulsion copolymerization |
US20020111435A1 (en) * | 2000-10-06 | 2002-08-15 | Hans-Erich Gasche | Process for the preparation of graft rubber latexes having a reduced residual monomer content |
KR20090052364A (ko) * | 2006-08-18 | 2009-05-25 | 바스프 에스이 | 아크릴로니트릴, 스티렌 및 부타디엔 기재의 열가소성 성형조성물 |
KR20120061173A (ko) * | 2010-12-02 | 2012-06-13 | 금호석유화학 주식회사 | 열안정성이 우수한 그라프트 공중합체 라텍스의 제조 방법 |
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0003957B1 (en) * | 1978-03-03 | 1982-09-29 | Isr Holding S.A.R.L. | Process for reducing the residual styrene level of a polystyrene latex |
US4703090A (en) * | 1984-12-18 | 1987-10-27 | Enichem Polimeri S.P.A. | Method for the preparation of graft copolymers by emulsion copolymerization |
US20020111435A1 (en) * | 2000-10-06 | 2002-08-15 | Hans-Erich Gasche | Process for the preparation of graft rubber latexes having a reduced residual monomer content |
KR20090052364A (ko) * | 2006-08-18 | 2009-05-25 | 바스프 에스이 | 아크릴로니트릴, 스티렌 및 부타디엔 기재의 열가소성 성형조성물 |
KR20120061173A (ko) * | 2010-12-02 | 2012-06-13 | 금호석유화학 주식회사 | 열안정성이 우수한 그라프트 공중합체 라텍스의 제조 방법 |
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