Thermoplastic polyester resin composition and molded article
A technology of thermoplastic polyester and resin composition, which is applied in the field of thermoplastic polyester resin composition, can solve the problems of insufficient heat aging resistance and mechanical physical properties, and increase the amount of gas, and achieve excellent heat aging resistance and dimensional stability , Low gas performance and excellent exudation effect
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Embodiment 1~21、 comparative example 1~4
[0174] Using a twin-screw extruder (Nippon Steel Works, TEX-30α) with a screw diameter of 30 mm, a ratio of 20% of the kneading area, and L / D35 rotating in the same direction, (A-1) was polymerized. Butylene phthalate resin, (B) a polyol compound having 5 or more hydroxyl groups or (B') a polyol compound other than the above (B), and (C) a polyfunctional epoxy compound are listed in Table 1- The compositions shown in 3 and 5 were mixed and added from the main feed section of the twin-screw extruder. Furthermore, melt-mixing was performed on the extrusion conditions of 250 degreeC of kneading temperature and 150 rpm of screw rotation speed, and the obtained resin composition was discharged in the form of a strand. After passing the discharged resin composition through a cooling bath, it was granulated with a wire cutter.
[0175] In Examples 1 to 14, the obtained pellets were dried in a hot air dryer at a temperature of 110° C. for 12 hours, and then evaluated by the metho...
Embodiment 22
[0177] (A-2) Polyparaphenylene Ethylene glycol diformate resin, (B) polyols having 5 or more hydroxyl groups, and (C) polyfunctional epoxy compounds are mixed according to the composition shown in Table 4, and added from the main feed section of the twin-screw extruder . Furthermore, melt-mixing was performed on the extrusion conditions of 280 degreeC of kneading temperature and 150 rpm of screw rotation speed, and the obtained resin composition was discharged in the form of a strand. After passing the discharged resin composition through a cooling bath, it was granulated with a wire cutter.
[0178] The obtained pellets were dried in a hot air dryer at a temperature of 150° C. for 3 hours, and then evaluated by the methods described in the above items 1. to 6.
Embodiment 23、24、25、 comparative example 5~7
[0180] Using a twin-screw extruder (Nippon Steel Works, TEX-30α) with a screw diameter of 30 mm, a ratio of 20% of the kneading area, and L / D35 rotating in the same direction, (A-1) was polymerized. Butylene phthalate resin, (B) a polyhydroxy compound having 5 or more hydroxyl groups or (B') the above-mentioned polyhydroxy compound except (B), and (C) a polyfunctional epoxy compound according to Table 4 and The containing composition shown in Table 5 was mixed, and it added from the main feed part of a twin-screw extruder. (D) The inorganic filler was added from between the main feed part and the vent part using a side feeder according to the composition shown in Table 4 and Table 5. Melt mixing was carried out under the extrusion conditions of a kneading temperature of 250° C. and a screw rotation speed of 150 rpm, and the obtained resin composition was discharged in a strand form. After passing the discharged mixture through a cooling bath, granulation was performed using...
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