Polyphenylene ether-based resin composition
A resin composition and styrene-based resin technology, applied in the field of polyphenylene ether-based resin compositions, can solve problems such as difficulties, not necessarily sufficient effects, and becoming flame retardant, and achieve excellent flame retardancy, excellent mechanical strength, Excellent lightweight effect
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[0169] The present invention will be described below with reference to specific examples and comparative examples. The invention is not limited to these examples.
[0170] The measurement methods and raw materials for the physical properties used in Examples and Comparative Examples are as follows.
[0171] (1. specific gravity)
[0172] The specific gravity of the polyphenylene ether resin composition manufactured in the Example and the comparative example was measured using the electronic density meter SD-200L by Alfa Mirage.
[0173] As an evaluation criterion, the smaller the specific gravity, the better the lightness and the like.
[0174] (2. Volume resistivity)
[0175] The pellets of the polyphenylene ether-based resin compositions produced in Examples and Comparative Examples were dried in a hot air dryer at 90° C. for 1 hour. Using an injection molding machine (IS-80EPN, manufactured by Toshiba Machine Co., Ltd.) equipped with a dot-gate flat mold with a size of ...
Embodiment 1
[0211] By TEM58SS twin-screw extruder (manufactured by Toshiba Machinery Co., Ltd., barrel number 13, screw diameter 58mm, L / D=53; There are 2 kneading discs L, 14 kneading discs R and 2 kneading discs N The most upstream part (top feed port) of the screw mode) supplies (PPE1) 58 mass parts, (HIPS) 10 mass parts, (GPPS) 5 mass parts, and uses the liquid addition device and the liquid addition nozzle to add from the barrel 4 in the middle. 18 parts by mass of liquid feed (FR), 9 parts by mass of feed (CF1) from 8 sides of the barrel in the middle, at a barrel temperature of 300°C, a screw speed of 400rpm, an extrusion rate of 400kg / hr, and a vacuum degree of the exhaust port of 7.998 Melt-kneading was performed under the condition of kPa (60 Torr) to obtain a resin composition. The physical property measurement results of the obtained resin composition are listed in Table 1 below.
Embodiment 2
[0213] By TEM58SS twin-screw extruder (manufactured by Toshiba Machinery Co., Ltd., barrel number 13, screw diameter 58mm, L / D=53; There are 2 kneading discs L, 14 kneading discs R and 2 kneading discs N The most upstream part (top feed port) of the screw mode) supplies 50 parts by mass of (PPE1) and 25 parts by mass of (PPE2), and uses a liquid addition device and a liquid addition nozzle to add liquid feed (FR) 16 from the barrel 4 in the middle Parts by mass, feed (CF1) 9 parts by mass from the 8 sides of the barrel in the middle, under the conditions of barrel temperature 300°C, screw speed 400rpm, extrusion rate 400kg / hr, and exhaust port vacuum 7.998kPa (60Torr) Melt-kneading was performed to obtain a resin composition. The physical property measurement results of the obtained resin composition are listed in Table 1 below.
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Abstract
Description
Claims
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