Styrenic resin composition for optics, molded article, and light guide plate
A styrene-based resin and styrene-based technology, applied in the field of styrene-based resin compositions, can solve problems such as chromaticity changes, backlight brightness reduction, and yellowing of molded products, achieving small changes in hue and transmittance, High coloring prevention effect, excellent colorless transparency effect
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Embodiment 1-1~1-25
[0118] (Examples 1-1 to 1-25, Comparative Examples 1-1 to 1-8, Reference Examples 1-1 to 1-9)
[0119] With the content shown in Table 2, using a screw diameter of 40mm single-screw extruder, styrenic resins PS-1, PS-2, PS-3 and B, C, and D as additives at the barrel temperature Melt kneading at 230° C. and a screw rotation speed of 100 rpm to obtain granules. The additives used in Table 2 are as follows. Here, additive B represents (b) 6-[3-(3-tert-butyl-4-hydroxy-5-methylphenyl)propoxy]-2,4,8,10-tetra-tert-butyl Benzo[d,f][1,3,2]dioxaphosphopane, additive C means (c) phosphorus antioxidant, additive D means (d) hindered phenolic antioxidant.
[0120] B: 6-[3-(3-tert-butyl-4-hydroxy-5-methylphenyl)propoxy]-2,4,8,10-tetra-tert-butylbenzo[d,f] [1,3,2] Dioxaphosphopane (SUMILIZER GP manufactured by Sumitomo Chemical Co., Ltd.)
[0121] C-1: Tris(2,4-di-tert-butylphenyl)phosphite (Irgafos168 manufactured by BASF Japan Co., Ltd.)
[0122] C-2: 2,2'-methylenebis(4,6-di-tert-bu...
Embodiment 2-1~2-34
[0150] The first reactor and the second reactor as a complete mixing type stirred tank and the third reactor as a plug flow type reactor with a static mixer are connected in series to constitute a polymerization process, as shown in Table 1. Production of the styrene-based resin was carried out under Condition 1 shown. The capacity of each reactor was 39 liters for the first reactor, 39 liters for the second reactor, and 16 liters for the third reactor. A raw material solution was prepared using the raw material composition described in Condition 1 of Table 1, and the raw material solution was continuously supplied to the first reactor at the flow rate described in Table 1.
[0151] Moreover, at the inlet of the 3rd reactor, the hydrophilic additive E which has a polyether chain was added so that it might become the kind and content shown in Table 3. The kinds of additives and polyethylene glycols used are as follows.
[0152] E-1: Polyethylene glycol with an average molecul...
Embodiment 3-1~3-10
[0175] The first reactor and the second reactor as a complete mixing type stirred tank and the third reactor as a plug flow type reactor with a static mixer are connected in series to constitute a polymerization process, as shown in Table 4. Production of the styrene-based resin was carried out under the conditions shown. The capacity of each reactor was 39 liters for the first reactor, 39 liters for the second reactor, and 16 liters for the third reactor. A raw material solution was prepared using the raw material composition described in Table 4, and the raw material solution was continuously supplied to the first reactor at the flow rate described in Table 4. At the inlet of the first reactor, a polymerization initiator was added to the raw material solution so as to have the addition concentration (mass basis relative to the total amount of raw material styrene and methacrylic acid) described in Table 4, and uniformly mixed. The polymerization initiator that table 4 recor...
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