Preparation method of thermotropic liquid crystal polyarylate
A technology of thermotropic liquid crystal and polyarylate, applied in the field of preparation of thermotropic liquid crystal polyarylate, can solve the problems of short reaction time and large shearing force, achieve sufficient material contact, shorten production cycle, and overcome product quality unstable effect
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Embodiment 1
[0022] Add p-acetoxybenzoic acid and 6-acetoxy-2-naphthoic acid in a molar ratio of 75:25 into the polymerization tank, keep at 180°C for 2h, then raise the temperature to 250°C for 1h, nitrogen flow rate is 50ml / min, Prepare the prepolymer; after preheating the prepolymer at 120°C for 1min, react at 200°C and 20KPa vacuum for 5min, the viscosity-increasing reaction occurs, and then continue the viscosity-increasing reaction at 300°C with a vacuum of 50KPa After 20 minutes, the liquid crystal polyester was directly extruded through a die to obtain a thermotropic liquid crystal polyarylate with a weight average molecular weight of 29,500.
Embodiment 2
[0024] Add p-acetoxybenzoic acid, terephthalic acid, and m-diacetoxybenzene in a molar ratio of 50:25:25 to the polymerization kettle, keep it at 210°C for 1.5h, then raise the temperature to 250°C and keep it for 1h, the nitrogen flow rate is 50ml / min to prepare the prepolymer; transport the prepolymer to the screw extruder, after preheating at 120°C for 1min, react at a temperature of 220°C and 20KPa vacuum for 5min, a viscosifying reaction occurs, and then at 320°C The viscosity-increasing reaction was continued for 25 minutes at a vacuum degree of 50KPa, and finally the liquid crystal polyester was directly extruded through a die to obtain a thermotropic liquid crystal polyarylate with a weight average molecular weight of 36,000.
Embodiment 3
[0026] Add p-acetoxybenzoic acid, isophthalic acid, and 1,4-diacetoxynaphthalene in a molar ratio of 60:20:20 to the polymerization kettle, keep at 200°C for 3h, then raise the temperature to 250°C for 1.5h, The nitrogen flow rate is 50ml / min, and the prepolymer is prepared; the prepolymer is transported to the screw extruder, and after being preheated at 150°C for 1min, it is reacted at a temperature of 220°C and a vacuum condition of 30KPa for 8min, and a viscosity-increasing reaction occurs. Afterwards, the viscosity-increasing reaction was continued for 20 minutes at 350° C. under a vacuum of 40 KPa, and finally the liquid crystal polyester was directly extruded through a die to obtain a thermotropic liquid crystal polyarylate with a weight average molecular weight of 36,000.
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