Defoaming method of carbon fiber spinning dope
A carbon fiber and defoaming technology, used in fiber processing, filament forming processing, textiles and papermaking, etc., can solve the problem of difficult removal of air bubbles, and achieve the effect of inhibiting decomposition reaction, good technical effect, and transparent color.
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Embodiment 1
[0015] Through solution polymerization, in the stock solution obtained by copolymerization of acrylonitrile and itaconic acid, the weight ratio of acrylonitrile monomer / copolymer / DMSO is 3% / 17% / 80%, and the initiator used in the polymerization process is azobis Isobutyronitrile, the polymerization reaction temperature is 60°C, and the polymerization tank is 5L. After the reaction is finished, vacuumize and remove the singles, and the content of acrylonitrile after the singles is removed is 1500ppm. The spinning dope after de-singing is subjected to defoaming treatment, first vacuumed for 10 minutes, the pressure is -0.1MPa, and then nitrogen gas is introduced until the pressure is 0.03MPa, the nitrogen purity is 99.999% and the temperature is 55°C. After standing still for 20 hours, test the bubble content of the stock solution, the number of bubbles shown under the microscope is 3, and there is no loss of solvent.
Embodiment 2
[0019] Through solution polymerization, in the stock solution obtained by copolymerization of acrylonitrile and methyl acrylate, the weight ratio of acrylonitrile monomer / copolymer / NaSCN aqueous solution is 10% / 20% / 70%, and the initiator used in the polymerization process is azo Diisobutyronitrile, the polymerization reaction temperature is 80°C, and the polymerization tank is 5L. After the reaction is finished, vacuumize and remove the singles. After the singles are removed, the acrylonitrile content is 2000ppm. The spinning dope after de-singing is subjected to defoaming treatment, first vacuumed for 30 minutes, the pressure is -0.06MPa, and then nitrogen gas is introduced until the pressure is 0.01MPa, the nitrogen purity is 99% and the temperature is 75°C. After standing still for 28 hours, the bubble content of the stock solution was tested, and observation under the microscope showed that the number of bubbles was 0, and there was no loss of solvent.
Embodiment 3
[0023] Through solution polymerization, in the stock solution obtained by copolymerization of acrylonitrile, itaconic acid and methyl acrylate, the weight ratio of acrylonitrile monomer / copolymer / DMSO is 8% / 18% / 74%, and the initiator used in the polymerization process It is azobisisoheptanonitrile, the polymerization reaction temperature is 45°C, and the polymerization tank is 5L. After the reaction is finished, vacuumize and remove the singles. After the singles are removed, the acrylonitrile content is 1000ppm. The spinning dope after de-singling is subjected to defoaming treatment, first vacuumed for 60 minutes, the pressure is -0.08MPa, and then argon gas is introduced until the pressure is 0.15MPa, the purity of the argon gas is 97% and the temperature is 40°C. After standing still for 28 hours, the bubble content of the stock solution was tested, and observation under the microscope showed that the number of bubbles was 2, and there was no loss of solvent.
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