Semi-continuous preparation method for solution of heterocycle-containing aromatic polyamide copolymer
A semi-continuous technology for aromatic polyamides, which is applied in the field of semi-continuous preparation of heterocyclic-containing copolymerized aromatic polyamide solutions, which can solve the problems of low molecular weight of polymerization products, uneven solution, difficult mass transfer and heat transfer of the system, etc. , to achieve the effect of improving uniformity, increasing molecular weight and reducing side reactions
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Embodiment 1
[0028] In a kettle reactor, 4.76 parts of lithium chloride were dissolved in 158 parts of freshly distilled dry DMAc to prepare a mixed solvent, and 1 part of refined PPDA and 3.1 parts of M3 were dissolved in it at -10°C, Then add 4.7 parts of refined TPC for pre-polycondensation, keep the temperature of the system below 10°C, after 30 minutes of reaction, a low-molecular-weight prepolymer is formed. Screw extruder. The temperature of the twin-screw extruder was controlled at 80° C., and a light yellow transparent polymer solution was extruded for about 18 minutes. The inherent viscosity of the polymer was determined to be 6.5 dL / g, and the solution concentration was 4.1%.
Embodiment 2
[0030] In a kettle reactor, 4.2 parts of lithium chloride were dissolved in 141 parts of freshly distilled dry DMAc to prepare a mixed solvent, and 1 part of refined PPDA and 2.54 parts of M3 were dissolved in it at -10°C, Then add 4.18 parts of refined TPC for pre-polycondensation, keep the temperature of the system below 10°C, and react for 30 minutes to generate a low-molecular-weight prepolymer. Screw extruder. The temperature of the twin-screw extruder was controlled at 80° C., and a light yellow transparent polymer solution was extruded for about 18 minutes. The inherent viscosity of the polymer was determined to be 6.3 dL / g, and the solution concentration was 4%.
Embodiment 3
[0032] In a kettle reactor, 3.8 parts of lithium chloride were dissolved in 127 parts of freshly distilled dry DMAc to prepare a mixed solvent, and 1 part of refined PPDA and 2.1 parts of M3 were dissolved in it at -10°C, Then add 3.76 parts of refined TPC for pre-polycondensation, keep the temperature of the system lower than 10 ° C, and react for 30 minutes to generate a low molecular weight prepolymer, which enters a double-stranded polymer with a diameter of 25 mm, an aspect ratio of 1:40, and a rotating speed of 50 rpm. Screw extruder. The temperature of the twin-screw extruder was controlled at 80° C., and a light yellow transparent polymer solution was extruded for about 18 minutes. The inherent viscosity of the polymer was determined to be 6.2 dL / g, and the solution concentration was 4%.
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