Direct fusion method for preparing poly lactic acid in high molecular weight
A high-molecular-weight polylactic acid technology, which is applied in the field of direct melting to prepare high-molecular-weight polylactic acid, can solve problems such as high cost polycondensation, inability to fully achieve the effect, and impure products
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Embodiment 1
[0024] Add 50ml of L-lactic acid with a content of 85% to a 250ml four-necked bottle equipped with a thermometer, a stirrer and a nitrogen inlet tube, feed nitrogen, heat to 110°C, and stir and dehydrate for 2 hours under a vacuum of 80mmHg; then , add 0.2 grams of stannous chloride, gradually increase the temperature from 110°C to 160°C, and polycondense for 10 hours under a vacuum of 10mmHg to obtain a lactic acid polymer with an intrinsic viscosity of 0.15dl / g; finally, add 1wt% (relative to the quality of lactic acid) 1,2 epoxy octanoyl chloride, reacted for 3 hours to obtain polylactic acid with an intrinsic viscosity of 1.1dl / g.
Embodiment 2~6
[0026] Based on Example 1, the chain extender is 1,2 epoxy octanoyl chloride, change the consumption of adding chain extender, obtain the following results:
[0027] The amount of chain extender (relative to the quality of lactic acid) Intrinsic viscosity of polylactic acid
[0028] 0.5wt% 0.8dl / g
[0029] 2wt% 1.4dl / g
[0030] 4wt% 1.1dl / g
[0031] 6wt% 0.65dl / g
[0032] 10wt% 0.4dl / g
Embodiment 8
[0034] Based on Example 1, first polymerize to obtain a lactic acid polymer with an intrinsic viscosity of 0.15dl / g, and then prepare high-molecular-weight polylactic acid by reactive extrusion, and the obtained polylactic acid has an intrinsic viscosity of 1.3dl / g. During the reactive extrusion process, 2 wt % (relative to the mass of lactic acid) of 1,2 epoxy octanoyl chloride was added, the vacuum degree was 50 mmHg, and the reactive extrusion was carried out under the condition of nitrogen flow, and the residence time in the extruder was 10 minutes.
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