A kind of production method of polylactic acid class material
A technology of polylactic acid and copolymer, which is applied in the field of production of biodegradable materials, can solve the problems of high energy consumption and long polymerization process, and achieve the effects of low energy consumption, simple process equipment and improved product quality
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Embodiment 1
[0040] Add 200kg of L-lactide to a 500L melting tank purged with nitrogen and at a temperature of 110°C. After the L-lactide is completely melted, it is continuously supplied to a 20L prepolymerization tank at a mass flow rate of 5kg / h by a metering pump. At the same time, the catalyst stannous octoate was continuously supplied to a 20L prepolymerization tank at a mass flow rate of 1.5g / h through a syringe pump, and prepolymerized at a temperature of 150°C and a pressure of 0.4MPa for 2.0 hours. The conversion rate of lactide reaches 50%.
[0041] The obtained prepolymer was sent to the tubular reactor with a gear pump, operated adiabatically and the residence time was 2.0 hours, the conversion rate of lactide was finally 96.6%, and the temperature of the melt rose to 185°C. The weight average molecular weight of the obtained polylactic acid material was 145,000. As shown in Table 1.
Embodiment 2
[0043] Add 200kg of DL-lactide to a 500L melting tank purged with nitrogen and at a temperature of 130°C. After the DL-lactide is completely melted, it is continuously supplied to a 20L prepolymerization tank at a mass flow rate of 5kg / h by a metering pump At the same time, the catalyst stannous octoate was continuously supplied to a 20L prepolymerization tank at a mass flow rate of 1.5g / h through a syringe pump, and prepolymerized at a temperature of 150°C and a pressure of 0.4MPa for 2.0 hours. The lactide conversion rate reached 45%.
[0044] The obtained prepolymer was sent to the tubular reactor with a gear pump, operated adiabatically and the residence time was 2.0 hours, the conversion rate of lactide was finally 96.4%, and the temperature of the melt rose to 188°C. The weight average molecular weight of the obtained polylactic acid material was 155,000. As shown in Table 1.
Embodiment 3
[0046] Add 200kg of L-lactide to a 500L melting tank purged with nitrogen and at a temperature of 110°C. After the L-lactide is completely melted, 20L of pre-polymerized At the same time, the catalyst stannous octoate was continuously supplied to a 20L prepolymerization kettle at a mass flow rate of 1.0 g / h through a syringe pump, and the prepolymerization was carried out at a temperature of 140° C. and a pressure of 0.4 MPa for 2.5 hours. The conversion rate of lactide reaches 40%.
[0047] The obtained prepolymer was sent to the tubular reactor with a gear pump, operated adiabatically and the residence time was 3.0 hours, the conversion rate of lactide was finally 96.3%, and the temperature of the melt rose to 190°C. The weight average molecular weight of the obtained polylactic acid material was 149,000. As shown in Table 1.
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