Method for removing acrylonitrile monomer in spinning solution
A technology for spinning dope and acrylonitrile, applied in the field of acrylonitrile monomer removal, can solve problems such as skinning of spinning dope, and achieve the effects of reducing residual amount, alleviating the phenomenon of skinning, and avoiding a large amount of extraction
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Embodiment 1
[0023] Through solution polymerization, in the stock solution obtained by the copolymerization of acrylonitrile and itaconic acid, the ratio of acrylonitrile monomer / copolymer / DMSO is 3% / 17% / 80%, and the initiator used in the polymerization process is azobisiso Butyronitrile, the polymerization reaction temperature is 60°C, and the polymerization tank is 5L. After the reaction is finished, vacuumize and remove the sheets. The vacuum degree is 50mbar. After 15 minutes of vacuuming, nitrogen gas is introduced to normal pressure. The nitrogen gas first passes through the preheating device, and the preheating temperature is 55°C. Stir during nitrogen flow, the stirring rate is 50 rpm, and continue to vacuumize after 10 minutes. After repeating this 4 times, the residual single content in the measured mixture is 800ppm.
Embodiment 2
[0027] Through solution polymerization, in the stock solution obtained by copolymerization of acrylonitrile and methyl acrylate, the ratio of acrylonitrile monomer / copolymer / DMSO is 10% / 20% / 70%, and the initiator used in the polymerization process is azodiiso Butyronitrile, the polymerization reaction temperature is 58°C, and the polymerization tank is 5L. After the reaction is finished, vacuumize and remove the sheets. The vacuum degree is 120mbar. After 18 minutes of vacuuming, nitrogen gas is introduced to normal pressure. The nitrogen gas first passes through the preheating device, and the preheating temperature is 55°C. Stir during nitrogen flow, the stirring rate is 180 rpm, and continue to vacuumize after 15 minutes. After repeating this for 3 times, the residual single content in the measured mixture is 600ppm.
Embodiment 3
[0031]Through solution polymerization, in the stock solution obtained by copolymerization of acrylonitrile, itaconic acid and methyl acrylate, the ratio of acrylonitrile monomer / copolymer / DMSO is 8% / 18% / 74%, and the initiator used in the polymerization process is Azobisisoheptanonitrile, the polymerization reaction temperature is 45°C, and the polymerization tank is 5L. After the reaction is finished, vacuumize and remove singletons. The vacuum degree is 80mbar. After evacuating for 18 minutes, nitrogen gas is introduced to normal pressure. The nitrogen gas first passes through the preheating device, and the preheating temperature is 40°C. Stir during nitrogen flow, the stirring rate is 15 rev / min, and continue to vacuumize after 8 minutes. After repeating this 6 times, the residual single content in the measured mixture is 400ppm.
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