초고 흐름 아크릴로니트릴 부타디엔 스티렌 코폴리머 조성물

    公开(公告)号:KR20200143702A

    公开(公告)日:2020-12-24

    申请号:KR20207031814

    申请日:2019-04-12

    Abstract: 본발명은, (a) 50 내지 80 중량%의 SAN 코폴리머(a)(S/AN-비율 78:22 내지 65:35, Mw 80,000 내지 250,000); (b) 15 내지 60 중량%의그라프트쉬쓰(b2)와 40 내지 85 중량%의그라프트기재 - 응집된부타디엔고무라텍스 - (b1)로이루어지며, 응집된부타디엔고무라텍스(b1)(150 내지 800 nm의 D50)의존재하에 SAN을유화중합시킴으로써얻어지는 8 내지 25 중량%의그라프트코폴리머(b); 및 (c) 디엔/비닐아렌테이퍼드폴리머블록을포함하는 8 내지 30 중량%의 SBC 블록코폴리머(비닐아렌 58 내지 68 중량%)를포함하고; 우수한기계적특성을갖는초고용융흐름을나타내는열가소성성형조성물, 이들의제조공정및 부피가크고/거나얇은벽 물품의생산을위한이들의사용에관한것이다.

    가공성과 표면 품질의 우수한 특성 조합을 갖는 ABS 성형 화합물
    2.
    发明公开
    가공성과 표면 품질의 우수한 특성 조합을 갖는 ABS 성형 화합물 审中-公开
    ABS模塑料,加工性和表面质量优异结合

    公开(公告)号:KR20180006415A

    公开(公告)日:2018-01-17

    申请号:KR20177035544

    申请日:2016-05-12

    Inventor: MICHELS GISBERT

    Abstract: 본발명은그라프트고무 P-I 및 P-II를포함하는각각의에멀션의혼합물의공침에의해서가공되는적어도두 가지의그라프트고무 P-I 및 P-II를함유한열가소성성형화합물 F에관한것이다. 본발명은추가로그러한열가소성성형화합물 F을생산하는방법및 본발명에따른열가소성성형화합물 F로부터얻은성형체에관한것이다.

    Abstract translation: 本发明涉及一种接枝橡胶P-I和P-II,至少两个所述接枝橡胶P-I和含有P-II的热塑性模塑化合物F由每个所述乳液包括:a的混合物的共沉淀处理的。 本发明涉及本发明的用于制造这样的热塑性模塑化合物F进一步根据方法F由热塑性模塑料而得到的模塑制品,和。

    PROCESS FOR PRODUCING A THERMOPLASTIC MOULDING COMPOUND COMPRISING A THERMOPLASTIC COPOLYMER A AND A GRAFT COPOLYMER B

    公开(公告)号:US20240218090A1

    公开(公告)日:2024-07-04

    申请号:US18546728

    申请日:2022-02-15

    Inventor: Wolfgang FISCHER

    Abstract: The invention relates to a process for producing a thermoplastic moulding compound comprising a thermoplastic copolymer A and a graft copolymer B (4), comprising: continuously drying the dewatered graft copolymer B (4) by supplying a drying gas (3) and the dewatered graft copolymer B (4), by moving the dewatered graft copolymer B (4) through the drying gas (3) and forming a fluidized bed (5), the drying gas (3) having a feed temperature TG,feed in the range from 50° C. to 160° C., and by removing dried graft copolymer B (4) and an offgas (7), wherein i. a starting temperature Tin of the fluidized bed (5) on feeding (9) of the dewatered graft copolymer B (4) is measured, ii. a finish temperature Tout of the fluidized bed (5) on removal (11) of the dried graft copolymer B (4) and/or of the offgas (7) is measured, iii. a difference ΔTact between the finish temperature Tout and the starting temperature Tin is formed and the difference ΔTact is compared with a target value ΔTtarget, and iv. the finish temperature Tout is adjusted by—increasing a mass flow rate of drying gas (3) supplied and/or the feed temperature TG,feed of the drying gas (3) when the difference ΔTact is smaller than the target value ΔTtarget or—reducing a mass flow rate of drying gas (3) supplied and/or the feed temperature TG,feed of the drying gas (3) when the difference ΔTact is greater than the target value ΔTtarget.

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