Continuous preparation method of polyhydroxy acid with high molecular weight
A technology of polyhydroxy acid and high molecular weight, which is applied in the field of continuous preparation of polyhydroxy acid, can solve the problems of deep coloring of products, long polymerization reaction time, difficult removal of materials, etc., and achieve less coloring, excellent melt stability, strength and The effect of keeping the shape for a long time
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Embodiment 1
[0067] Take 1000g of high-purity glycolide, add 50ppm of SnCl 2 2H 2 O, the two are mixed evenly with a pulverizer and then fed into the screw stirring reactor through the feeding funnel at a constant speed, and the feeding speed is kept consistent with the discharging speed. The reactor includes a total of 6 heating zones (e.g. Figure 5 As shown, that is, n=6), the temperature of each zone is set separately in advance. The reactor is set up as follows:
[0068] Feeding rate: 1kg / h; screw speed: 10rpm;
[0069] Reactor temperature: Zones 1 and 2 = 200°C; Zones 3 and 4 = 210°C; Zones 5 and 6 = 190°C;
[0070] The residence time is 10 minutes, the molecular weight average weight of the obtained polyglycolide is 180000, the molecular weight distribution range is 2.5; the yellowness index (YI) is 25.6; the melt viscosity is 500Pa·s.
Embodiment 2
[0072] Get the same glycolide 1000g of the purity in embodiment 1, add the SnCl of 500ppm 2 2H 2 O, the two are mixed evenly with a pulverizer and then fed into the screw stirring reactor through the feeding funnel at a constant speed, and the feeding speed is kept consistent with the discharging speed. The reactor is set up as follows:
[0073] Feeding rate: 1kg / h; screw speed: 30rpm;
[0074] Reactor temperature: Zones 1 and 2 = 210°C; Zones 3 and 4 = 220°C; Zones 5 and 6 = 190°C
[0075] The residence time is 3 minutes, the weight average molecular weight of the obtained polyglycolide is 250000, the molecular weight distribution range is 1.8; the yellowness index (YI) is 28.8; the melt viscosity is 620Pa·s.
Embodiment 3
[0077] Get the same glycolide 1000g of the purity in embodiment 1, add the SnCl of 2000ppm 2 2H 2 O, the two are mixed evenly with a pulverizer and then fed into the screw stirring reactor through the feeding funnel at a constant speed, and the feeding speed is kept consistent with the discharging speed. The reactor is set up as follows:
[0078] Feeding rate: 1kg / h; screw speed: 80rpm;
[0079]Reactor temperature: Zones 1 and 2 = 210°C; Zones 3 and 4 = 220°C; Zones 5 and 6 = 190°C
[0080] The residence time is 1.0 min, the weight average molecular weight of the obtained polyglycolide is 245000, the molecular weight distribution range is 2.0; the yellowness index (YI) is 47.1; the melt viscosity is 610Pa·s.
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