Polycarbonate resin composition comprising plant-derived component
A technology of resin composition and polycarbonate, applied in the field of resin composition, can solve problems such as difficulty
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[0060] Hereafter, although an Example demonstrates this invention concretely, this invention is not limited to these examples.
[0061] (Component A) polycarbonate component (hereinafter, sometimes abbreviated as "Bio-PC") and (Component B) polylactic acid component were produced by the method shown in the following production example. On the other hand, each value in the examples was determined by the following method.
[0062] (1) Reduction viscosity: The viscosity at 35° C. of a solution obtained by dissolving 120 mg of polycarbonate in 10 ml of a mixed solvent of phenol / tetrachloroethane (50 / 50 by volume) was measured with an Ubbelohde viscometer. The unit is dl (1 / 10 liter) / g.
[0063] (2) Weight average molecular weight: The weight average molecular weight of polylactic acid was calculated|required as the value converted into polystyrene by the gel permeation chromatography (GPC).
[0064] (3) The glass transition temperature and the ratio of the melting peak above 195...
manufacture example 1
[0076] Production example 1: (Component A) Production of polycarbonate component (Bio-PC)
[0077] Isosorbide (20.0kg, 137 moles), 1,3-propanediol (4.69kg, 61.6 moles) and diphenyl carbonate (41.9kg, 196 moles) were charged into the polymerization tank, and 2 , 2-bis(4-hydroxyphenyl)propane disodium salt (13.3mg, 4.89×10 -5 mol) and tetramethylammonium hydroxide (7130mg, 1.96×10 -2 mol), melted at 180°C under a nitrogen atmosphere. The pressure was reduced and the temperature was raised while stirring, and the inside of the reaction tank was adjusted to 66.67 Pa (0.5 mmHg) and 245° C. while distilling off generated phenol. The obtained polycarbonate is abbreviated as "Bio-PC".
[0078] The reduced viscosity of Bio-PC is 0.59-0.63, and the glass transition point measured by DSC is 121-122°C.
manufacture example 2
[0079] Production Example 2: Production of (B-1 component) poly-L-lactic acid component
[0080] Add 48.75 parts by weight of L-lactide (manufactured by Musashino Chemical Research Institute Co., Ltd.) and 1.25 parts by weight of D-lactide (manufactured by Musashino Chemical Research Institute Co., Ltd.) into the polymerization tank, and replace the system with nitrogen. , add 0.05 parts by weight of stearyl alcohol, tin octoate 25×10 as catalyst -3 parts by weight, polymerized at 190° C. for 2 hours to produce a polymer. This polymer was washed with a 7% 5N hydrochloric acid solution in acetone to remove the catalyst to obtain a poly-L-lactic acid component (PLLA, component B-1). The weight average molecular weight of the obtained PLLA (component B-1) was 118,200. The melting point (Tm) was 159°C. The crystallization point (Tc) was 120°C.
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