Polystyrene resin composition and light guide plate obtained by molding the resin composition
一种苯乙烯系树脂、组合物的技术,应用在导光板领域,能够解决光线透射率差、尚未完成聚苯乙烯系树脂光学特性、光线透射率低等问题,达到吸水性低的效果
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Embodiment 1
[0125]
[0126] 0.05 parts by mass of 1,1-bis(tert-butylperoxy)cyclohexane was added to 100 parts by mass of a mixed solution of 85 mass % of styrene (TBC concentration 11 μg / g) and 15 mass % of ethylbenzene. The polymerization solution was continuously charged into a 5.4-liter complete mixing reactor at a rate of 0.70 liter / hour, and the temperature was adjusted to 101°C. Next, the obtained solution was continuously charged into a 3.0-liter laminar flow reactor equipped with a stirrer and capable of temperature control in three zones. The temperature of the laminar flow reactor was adjusted to 113°C / 121°C / 128°C. A polymer solution was obtained in the above-mentioned manner.
[0127] The obtained polymer solution is continuously supplied to a devolatilization extruder with 2 stages of venting holes, and the temperature of the extruder is 225° C., and the vacuum degree of the 1st stage venting hole and the 2nd stage venting hole is 15 torr. The condition reclaims unreacted ...
Embodiment 2
[0130] Phosphorous antioxidant (tris(2,4-di-tert-butylphenyl) phosphite, trade name: Adecastab 2112) was added at a concentration of 0.10 parts by mass relative to 100 parts by mass of the polymer, and in addition, it was mixed with The same method as in Example 1 was used to obtain a polystyrene resin composition.
Embodiment 3
[0132] Added 0.01 part by mass of 1,1-bis(tert-butylperoxy)cyclohexane to 100 parts by mass of a mixed solution of 89 mass % of styrene (TBC concentration 11 μg / g) and 11 mass % of ethylbenzene The polymerization solution was continuously charged into a 5.4-liter complete mixing reactor at a rate of 0.70 liter / hour, and the temperature was adjusted to 117°C. Next, the obtained solution was continuously charged into a 3.0-liter laminar flow reactor equipped with a stirrer and capable of temperature control in three zones. The temperature of the laminar flow reactor was adjusted to 128°C / 135°C / 141°C. A polymer solution was obtained in the above-mentioned manner.
[0133] The obtained polymer solution is continuously supplied to a devolatilization extruder with 2 stages of venting holes, and the temperature of the extruder is 225° C., and the vacuum degree of the 1st stage venting hole and the 2nd stage venting hole is 15 torr. The conditions reclaim unreacted monomer and solve...
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