Liquid crystal polyester, molding composition composed of liquid crystal polyester and application of molding composition
A technology of molding composition and liquid crystal polyester, which is applied in the field of liquid crystal polyester and the molding composition composed of it, and can solve the problems affecting the application of liquid crystal polymer, mold filling dissatisfaction, resin fluidity, etc.
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Embodiment 1
[0066] Add the following monomer raw materials, acylating agent and catalyst to the polymerization reaction device equipped with agitator, reflux condenser, monomer feeding port, nitrogen inlet, thermometer and torque sensor.
[0067] (I) p-Hydroxybenzoic acid 911.7 g (66 mol %) HBA
[0068] (Ⅱ) 6-hydroxy-2-naphthoic acid 639.8 g (34mol%) HNA
[0069] Acylating agent: acetic anhydride 1020 g
[0070] Catalyst: Magnesium acetate 95mg
[0071] After the feeding is completed, completely replace the atmosphere in the reaction vessel with nitrogen, raise the temperature of the reaction system to 140°C under the protection of nitrogen, and keep the nitrogen pressure at 0.2MPa, and maintain this temperature for 2 hours to carry out the acylation reaction; After the reaction is over, turn on the vacuum pump to reduce the pressure in the reactor to 10KPa-30KPa, and quickly discharge acetic acid and unreacted acetic anhydride molecules from the rectification column to meet the process...
Embodiment 2-5
[0072] Embodiment 2-5: according to the formula of table 1, after the acylation reaction finishes, open vacuum pump and the pressure in the reactor is decompressed to 10KPa-30KPa, discharge acetic acid and unreacted acetic anhydride molecule rapidly from the rectifying column, to meet the rapid The process of heating requires that when the amount of acetic acid received reaches more than 50% of the theoretical value, the temperature should be raised to 210°C rapidly, and the reduced pressure condition should be maintained and the temperature of the reaction system should be raised to the highest temperature of 330°C within 6 hours. During this period, the acetic acid, especially Phenol and other by-product small molecules that cause molecular chain rearrangement and branching are then decompressed to 60KPa in 30 minutes; the rest are the same as in Example 1; the melting point, melt viscosity, and storage modulus release rate of the liquid crystal polyester are rod-shaped Fluid...
Embodiment 6-12
[0073] Embodiment 6-12: according to the formula of table 1, after the acylation reaction finishes, open vacuum pump and the pressure in the reactor is decompressed to 10KPa-30KPa, discharge acetic acid and unreacted acetic anhydride molecule rapidly from the rectifying column, in order to satisfy rapidly The process of heating up requires that when the amount of acetic acid received reaches more than 50% of the theoretical value, the temperature is raised to 220°C quickly, the reduced pressure condition is maintained and the temperature of the reaction system is raised to the highest temperature of 335°C within 6 hours, during which the acetic acid is continuously discharged, especially Phenol and other by-product small molecules that cause molecular chain rearrangement and branching are then decompressed to 70KPa in 30 minutes; the rest are the same as in Example 1; the melting point, melt viscosity, and storage modulus release rate of the liquid crystal polyester are rod-shap...
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