发明名称 Branched poly(arylene sulfide) resin and method for producing same
摘要 Disclosed are a branched poly(arylene sulfide) resin having a melt viscosity measured at a temperature of 310° C. and a shear rate of 1200 sec−1 of 65 to 450 Pa·s, a maximum draft ratio of 6500 or more, and a degree of whiteness of 65 or more; moreover, a branched poly(arylene sulfide) resin preferably having a dependence of melt viscosity on shear rate of 1.4 to 2.6 or a melt stability of 0.85 to 1.30; and a method for producing a branched poly(arylene sulfide) resin, wherein a sulfur source and a dihaloaromatic compound are caused to undergo a polymerization reaction at a temperature of 170 to 290° C. in the organic amide solvent in the presence of a polyhaloaromatic compound in an amount of 0.0001 to 0.01 mol per mol of the fed sulfur source.
申请公布号 US9255350(B2) 申请公布日期 2016.02.09
申请号 US201113638227 申请日期 2011.03.22
申请人 KUREHA CORPORATION 发明人 Taniguchi Shingo;Sakabe Hiroshi;Yoshida Yui;Sunagawa Kazuhiko
分类号 C08G75/16;C08G75/14;D01F6/76;C08G75/02;C08G75/00;B01D46/00;D04H1/42;D04H3/00 主分类号 C08G75/16
代理机构 Birch, Stewart, Kolasch & Birch, LLP 代理人 Birch, Stewart, Kolasch & Birch, LLP
主权项 1. A method for producing a branched poly(arylene sulfide) resin having characteristics (a) to (e) described below, wherein the method comprises causing a sulfur source and a dihaloaromatic compound to undergo a polymerization reaction, and wherein the polymerization reaction is one in which the sulfur source and the dihaloaromatic compound are caused to undergo a polymerization reaction at a temperature of 170 to 270° C. in an organic amide solvent, then at a time when the conversion of the dihaloaromatic compound has become 30% or more, a polyhaloaromatic compound in an amount of 0.0001 to 0.008 mol per mol of the fed sulfur source is added to a polymerization reaction mixture, at the same time or thereafter a phase separating agent is added, subsequently the temperature of the polymerization reaction mixture is raised, and then the polymerization reaction is continued at a temperature of 240 to 290° C.: (a) the melt viscosity measured at a temperature of 310° C. and a shear rate of 1200 sec−1 is 65 to 450 Pa·s; (b) the measured maximum draft ratio, VSD/V0, is 6500 or more, wherein the maximum draft ratio is measured by melting a dry polymer at 310° C., discharging the melted polymer at a discharging rate (V0) of 0.05 mm/min, and varying a take-up speed from 5 m/min to 500 m/min over 1 minute, and VSD is a rate at the time when the discharged material is broken; (c) the degree of whiteness is 65 or more; (d) the dependence of melt viscosity on shear rate, which is the ratio of a melt viscosity measured at a temperature of 310° C. and a shear rate of 200 sec−1 to a melt viscosity measured at a temperature of 310° C. and a shear rate of 1200 sec−1 is from 1.4 to 2.6; and (e) the melt stability, which is the ratio of a melt viscosity after retention at a temperature of 310° C. and a shear rate of 1200 sec−1 for 30 minutes to a melt viscosity after retention at a temperature of 310° C. and a shear rate of 1200 sec−1 for 5 minutes, is from 0.85 to 1.30.
地址 Tokyo JP