High-fluidity wholly aromatic liquid crystal polyester and preparation method thereof
A liquid crystal polyester and wholly aromatic technology, which is applied in the field of high fluidity wholly aromatic liquid crystal polyester and its preparation, can solve problems such as increased melt viscosity, difference in molecular weight of liquid crystal polyester, failure to fill, etc., to achieve fluidity Stable performance, high fluidity and uniform quality
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Embodiment 1
[0041] Add 2760g (20mol) p-hydroxybenzoic acid in the reactor that stirring device, thermometer and reflux condenser are installed, 1860g (10mol) 4,4-diphenol, 415g (2.5mol) isophthalic acid, 1245g ( 7.5 mol) terephthalic acid, 4284 g (42 mol) acetic anhydride, 5.28 g (0.04 mol) potassium phenate, after purging and replacing the air in the reactor with nitrogen, heat up to 140° C. for 2 hours to carry out the acetylation reaction. Then the temperature was raised to 340°C, during which the by-product acetic acid and unreacted acetic anhydride produced by the polymerization were discharged in time, and finally the vacuum was evacuated to 133Pa, and the vacuum was stopped until the stirring torque increased, and the material was pressed and discharged with nitrogen to obtain a prepolymer. The prepared prepolymer was crushed, solid-phase thickened under vacuum conditions, and kept at 240° C. for 18 hours to obtain a high-fluidity wholly aromatic liquid crystal polyester.
Embodiment 2
[0043] Add 2760g (20mol) p-hydroxybenzoic acid, 1880g (10mol) 2-hydroxyl-6-naphthoic acid, 4284g (42mol) acetic anhydride, 23.2g (0.2mol) in the reactor that stirrer, thermometer and reflux condenser are installed ) sodium phenate, after purging and displacing the air in the reactor with nitrogen, the temperature was raised to 140° C. for 2 hours to carry out the acetylation reaction. Then the temperature was raised to 340°C, during which the by-product acetic acid and unreacted acetic anhydride produced by the polymerization were discharged in time, and finally the vacuum was evacuated to 133Pa, and the vacuum was stopped until the stirring torque increased, and the material was pressed and discharged with nitrogen to obtain a prepolymer. The prepared prepolymer was crushed, solid-phase thickened under vacuum conditions, and kept at 250° C. for 8 hours to obtain a high-fluidity wholly aromatic liquid crystal polyester.
Embodiment 3
[0045] Add 3105g (22.5mol) p-hydroxybenzoic acid, 470g (2.5mol) 2-hydroxyl-6-naphthoic acid, 2325g (12.5mol) 4,4-linked Hydroquinone, 415g (2.5mol) isophthalic acid, 1660g (10mol) terephthalic acid, 5355g (52.5mol) acetic anhydride, 52.8g (0.4mol) potassium phenate, after nitrogen purging replaces the air in the reactor, Raise the temperature to 140° C. and keep it warm for 2 hours to carry out the acetylation reaction. Then the temperature was raised to 340°C, during which the by-product acetic acid and unreacted acetic anhydride produced by the polymerization were discharged in time, and finally the vacuum was evacuated to 133Pa, and the vacuum was stopped until the stirring torque increased, and the material was pressed and discharged with nitrogen to obtain a prepolymer. The prepared prepolymer was crushed, solid-phase thickened under vacuum conditions, and kept at 260° C. for 18 hours to obtain a high-fluidity wholly aromatic liquid crystal polyester.
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