A kind of method of producing poly-p-phenylene benzobisoxazole fiber
A technology of benzobisoxazole and polyparaphenylene, which is applied in the field of preparation of polyparaphenylenebenzobisoxazole fiber, can solve the problems of long time for removing hydrogen chloride, low solubility of terephthalic acid, long reaction time, etc. problem, to achieve the effect of high probability of direct collision, favorable polymer molecular weight, and accelerated reaction speed
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Embodiment 1
[0024] A) Preparation of pre-polymerization solution: 8.99 kg of terephthalic acid and 11.53 kg of 4,6-diaminoresorcinol hydrochloride were fully mixed in a nitrogen-filled ribbon mixer to form a mixed powder. Add 20kg of polyphosphoric acid solution with a mass percentage of phosphorus pentoxide of 73% into the reactor, and add the above-mentioned mixed powder together, connect the outlet of the lower part of the reactor to a multi-stage emulsification pump, and keep the temperature of the reactor at 40°C , grind and disperse continuously through multi-stage emulsification pump and vacuumize to remove hydrogen chloride for 180min at the same time. After removing the hydrogen chloride, continue to add 33kg of phosphorus pentoxide to the reaction kettle so that the mass percentage of phosphorus pentoxide in the polyphosphoric acid is adjusted to 83%, fully stir and keep the temperature at 180°C, and at the same time vacuumize and keep it for 270min, After the prepolymerization ...
Embodiment 2
[0027] A) Preparation of pre-polymerization solution: 8.99 kg of terephthalic acid and 11.53 kg of 4,6-diaminoresorcinol hydrochloride were fully mixed in an argon-filled ribbon mixer to form a mixed powder. Add 14kg of polyphosphoric acid solution with a mass percentage of phosphorus pentoxide of 73% into the reactor, and add the above-mentioned mixed powder together. The grinder continuously circulates to grind and disperse while vacuuming to remove hydrogen chloride for 180 minutes. After removing the hydrogen chloride, continue to add 30kg of phosphorus pentoxide to the reaction kettle so that the mass percentage of phosphorus pentoxide in the polyphosphoric acid is adjusted to 84%, stir well and keep the temperature at 160°C, and at the same time vacuumize and keep it for 180min, After the prepolymerization reaction is completed, the prepolymerization solution is transferred to the prepolymerization solution storage tank, and the polymer mass percentage in the prepolymeri...
Embodiment 3
[0030] A) Preparation of pre-polymerization solution: 8.99 kg of terephthalic acid and 11.53 kg of 4,6-diaminoresorcinol hydrochloride were fully mixed in a nitrogen-filled ribbon mixer to form a mixed powder. Add 12kg of polyphosphoric acid solution with a mass percentage of phosphorus pentoxide of 74% into the reactor, and add the above-mentioned mixed powder together. Grind and disperse continuously through a twin-screw pump while vacuuming to remove hydrogen chloride for 60 minutes. After removing the hydrogen chloride, continue to add 28kg of phosphorus pentoxide to the reaction kettle so that the mass percentage of phosphorus pentoxide in the polyphosphoric acid is adjusted to 84%, fully stir and keep the temperature at 150°C, and at the same time vacuumize and keep it for 180min, After the prepolymerization reaction is completed, the prepolymerization solution is transferred to the prepolymerization solution storage tank, and the polymer mass percentage in the prepolyme...
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