Aliphatic polyester copolymer and process for producing same, biodegradable resin molding based on aliphatic polyester, and lactone-containing resin
A technology of aliphatic polyester and manufacturing method, applied in Group IV involving biodegradable aliphatic polymer, Group VI involving lactone-containing resin, 03] the second field of the present invention, to achieve the effect of excellent impact resistance
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[0963] Hereinafter, Groups I to VII of the present invention will be specifically described by way of examples and comparative examples, but the present invention is not limited thereto.
[0964] Various measured values of the aliphatic polyester copolymers in Examples and Comparative Examples were obtained by the following methods.
[0965] (molecular weight and molecular weight distribution)
[0966] A standard curve was drawn from standard polystyrene by gel permeation chromatography (GPC), and the number average molecular weight (Mn), weight average molecular weight (Mw) and molecular weight distribution (Mw / Mn) were obtained. Chloroform was used as the eluent.
[0967] (acid value and hydroxyl value)
[0968] Measured in accordance with JIS K0070.
[0969] (thermal properties)
[0970] The melting point and glass transition temperature were determined by a differential scanning calorimeter (DSC).
[0971] (Mechanical strength)
[0972] The tensile elongation and s...
Embodiment I-1
[0980] In the pre-polymerization tank equipped with stirrer, fractional condenser and temperature regulating device, 2.91 kg of 1,4-butanediol, 3.63 kg of succinic acid and 0.62 kg of ε-caprolactone were added together. Here, [B] / [A]=1.05 in the aforementioned formula (i), and [C] / ([A]+[C])=0.15 in the aforementioned formula (ii).
[0981]4.37 g of tetraisopropyl titanate and 0.89 g of magnesium hydrogen phosphate trihydrate were added thereto, stirred under normal pressure at a temperature of 145-225° C., and esterified. When the amount of distillate exceeds 0.8 kg, the prepolymerization process is terminated, and the reaction liquid is moved to the polymerization tank. The reaction solution was stirred at a temperature of 220-240° C., finally depressurized to 1.0 mmHg (133 Pa), and stirred for 3 hours to carry out the glycol removal reaction (transesterification reaction). The obtained low molecular weight polyester (D) had a weight average molecular weight of 56,000 and an...
Embodiment I-2
[0986] In the pre-polymerization tank equipped with stirrer, fractional distillation condenser and temperature regulating device, 36.25 kilograms of 1,4-butanediol, 43.18 kilograms of succinic acid and 10.32 kilograms of ε-caprolactone were added together. Here, [B] / [A]=1.09 in the aforementioned formula (i), and [C] / ([A]+[C])=0.20 in the aforementioned formula (ii). Then, 52.01 g of tetraisopropyl titanate and 10.46 g of magnesium hydrogen phosphate trihydrate were added thereto, and stirred under normal pressure at a temperature of 145-225° C. to carry out esterification reaction. When the amount of the distillate exceeds 10.0 kg, the prepolymerization process is terminated, and the reaction liquid is moved to the polymerization tank. The reaction liquid was stirred at a temperature of about 230° C., finally depressurized to 1.0 mmHg (133 Pa), and stirred for 4 hours to carry out the glycol removal reaction (transesterification reaction). The obtained low molecular weight p...
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