Resin compositions and resin moldings
A technology of resin composition and polyester resin, applied in the field of resin composition and resin molded body, can solve the problems of reduced transparency, insufficient mechanical strength, reduced heat resistance, etc., and achieves good balance and stable retention of heat. Good properties and excellent hydrolysis resistance
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[0156] Hereinafter, although an Example demonstrates this invention in more detail, this invention is not limited to the following Example unless the summary is exceeded. The raw materials used in each of the following examples are as follows. In each of the following examples, the compounding amount refers to parts by weight.
[0157]
[0158] PC-1: bisphenol A type aromatic polycarbonate (manufactured by Mitsubishi Engineering Plastics (Engineering Plastics), "Iupilon (upilon) S-3000FN", viscosity average molecular weight 22500)
[0159] PC-2: bisphenol A type aromatic polycarbonate (manufactured by Mitsubishi Engineering Plastics, "Iupilon H-4000FN", viscosity average molecular weight 15500)
[0160] PC-3: bisphenol A type aromatic polycarbonate (manufactured by Mitsubishi Engineering Plastics, "Iupilon E-2000FN", viscosity average molecular weight 28000)
[0161]
[0162] PCC(A)-1: Alicyclic polyester resin described in Production Example 1 below
[0163] Intrinsic ...
manufacture example 1
[0192] 101.5 parts by weight of 1,4-cyclohexanedicarboxylic acid (the ratio of trans body:cis body is 96:4), 87.0 parts by weight of 1,4-cyclohexanedimethanol (trans body:cis body The ratio of 69:31) and 0.005 parts by weight of tetra-n-butyl titanate in 6% by weight butanol solution is charged into a capacity of 100 liters with agitator, distillation pipe, heating device, pressure gauge, thermometer and decompression device In a stainless steel reactor, the inside of the reactor was replaced with nitrogen. While sealing the inside of the reactor with nitrogen gas, the internal temperature was raised to 150° C. over 30 minutes, and then from 150° C. to 200° C. over 1 hour. Next, after maintaining at 200° C. for 1 hour to carry out esterification reaction, the temperature was raised from 200° C. to 250° C. over 45 minutes, and polycondensation reaction was carried out while gradually reducing the pressure in the reactor. Keep the pressure inside the reactor at an absolute pres...
manufacture example 2
[0194] Production Example 1 was carried out in the same manner as Production Example 1, except that the charged amount of 1,4-cyclohexanedimethanol was changed to 87.9 parts by weight, and the polycondensation reaction time was changed from 3.7 hours to 4.5 hours. The intrinsic viscosity and terminal carboxylic acid concentration were 0.841 dl / g and 2.7 equivalent / ton, respectively, YI (granule) = 13.8, and the melting point was 219.6°C.
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