Preparation method of full biodegradation polyester copolymer
A copolymer and fully degradable technology, applied in the field of preparation of biodegradable polyester copolymers, can solve the problem of few methods of polylactic acid toughness, and achieve the effects of excellent mechanical properties, simple process and easy industrial production.
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Embodiment 1
[0024] (1) Dehydrate 400gL-lactic acid in a reactor at 100°C, then add 20g of succinic acid, vacuumize, and carry out polycondensation reaction under the action of 0.5g of catalyst stannous octoate. The pressure in the reactor is 1000Pa , the temperature was 90°C, reacted for 10 hours, then lowered the pressure in the reactor to below 100Pa, raised the reaction temperature to 150°C, and continued to react for 15 hours to obtain M w =8×10 2 ~3.0×10 4 Carboxy-terminated lactic acid prepolymer;
[0025] (2) The carboxyl-terminated lactic acid prepolymer obtained in step (1) and 200g polypropylene carbonate diol (molecular weight 2000) are added in the reactor, vacuumize, logical N 2 Gas, carry out polymerization reaction; Reaction temperature is 150 ℃, reacts for 10 hours, namely obtains low molecular weight polylactic acid polycarbonate copolymer, and the weight average molecular weight of this product is M w 2×10 3 ~5×10 4 .
[0026] (3) low molecular weight polylactic ac...
Embodiment 2
[0028] (1) 800gL-lactic acid is dehydrated in a reactor at 110°C, then 40g of succinic acid is added, vacuumized, and polycondensation is carried out under the effect of 1g of catalyst stannous octoate, and the pressure in the reactor is 1500Pa, The temperature is 100°C, react for 2 hours, then reduce the pressure in the reactor to below 100Pa, raise the reaction temperature to 160°C, and continue the reaction for 10 hours to obtain M w =8×10 2 ~3.0×10 4 Carboxy-terminated lactic acid prepolymer;
[0029] (2) The carboxyl-terminated lactic acid prepolymer obtained in step (1) and 300g polycarbonate 1,6-hexanediol ester diol (molecular weight 3000) are added in the reactor, vacuumize, logical N 2 Gas, carry out polymerization reaction; Reaction temperature is 170 ℃, reacts for 10 hours, namely obtains low molecular weight polylactic acid polycarbonate copolymer, and the weight average molecular weight of this product is M w 2×10 3 ~5×10 4.
[0030] (3) low molecular weigh...
Embodiment 3
[0032] (1) 600gL-lactic acid is dehydrated in a reactor at 120°C, then 40g of succinic acid is added, vacuumized, and polycondensation is carried out under the action of 1g of catalyst stannous octoate, the pressure in the reactor is 1800Pa, The temperature is 120°C, react for 3 hours, then reduce the pressure in the reactor to below 100Pa, raise the reaction temperature to 170°C, and continue the reaction for 6 hours to obtain M w =8×10 2 ~3.0×10 4 Carboxy-terminated lactic acid prepolymer;
[0033] (2) The carboxyl-terminated lactic acid prepolymer obtained in step (1) and 400g polycarbonate 1,5-pentanediol-1,6-hexanediol ester (molecular weight 4000) are added in the reactor, vacuumize , through N 2 Gas, carry out polymerization reaction; Reaction temperature is 180 ℃, reacts for 8 hours, namely obtains low molecular weight polylactic acid polycarbonate copolymer, and the weight average molecular weight of this product is M w 2×10 3 ~5×10 4 .
[0034] (3) low molecul...
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