Prepn of polyacrylonitrile-base high-performance raw carbon fiber
A polyacrylonitrile-based, high-performance technology, applied in fiber chemical characteristics, textiles and papermaking, etc., can solve the problem of uneven heating of filaments, affecting the uniformity of the microstructure of the original silk, and the increase in the coefficient of variation of the mechanical properties of the original silk, etc. problem, achieve the effect of avoiding uneven heating, reducing the probability of occurrence, and reducing the solvent content
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Embodiment 1
[0023] 1. Preparation of spinning dope
[0024] Acrylonitrile, itaconic acid, and methyl methacrylate are blended at a weight ratio of 96:1:3 and then added to the reactor. Using dimethyl sulfoxide as a solvent, the temperature of the polymerization reaction is controlled at 75°C. The reaction time is 10 hours, and the PAN resin with a molecular weight of 140,000 and a molecular weight distribution of 3.5 is obtained by continuous polymerization, and the weight content of the PAN resin in the spinning dope is 20%.
[0025] 2. Filtration of silk stock solution The spinning stock solution is precisely filtered through a 5 μm filter material.
[0026] 3. The solidification of the silk stock solution is spun by dry-jet wet spinning. After the fiber leaves the spinneret hole, it enters the first-stage coagulation bath. The temperature of the first-stage coagulation bath is 0°C. The content of dimethyl sulfoxide in the coagulation bath It is 45wt%, and coagulation time is 2min. Aft...
Embodiment 2
[0037] 1. Preparation of silk stock solution
[0038]Acrylonitrile, itaconic acid, and methyl methacrylate are blended in a weight ratio of 92:2:6 and added to the reactor. By solution polymerization, using dimethyl sulfoxide as a solvent, the temperature of the polymerization reaction is controlled at 70°C. The reaction time is 20 hours, and the PAN resin with a molecular weight of 200,000 and a molecular weight distribution of 3.0 is obtained by continuous polymerization, and the weight content of the PAN resin in the silk stock solution is 23%.
[0039] 2. Filtration of spinning dope
[0040] The spinning dope is finely filtered through a 2.0μm filter material.
[0041] 3. Solidification and molding of the original solution
[0042] Adopt dry-jet wet-spinning method spinning, after fiber leaves spinneret orifice, enters first-stage coagulation bath, and first-stage coagulation bath temperature is 20 ℃, and the content of dimethyl sulfoxide in the coagulation bath is 65wt...
Embodiment 3
[0062] 1. Preparation of spinning dope
[0063] Acrylonitrile, itaconic acid, and methyl methacrylate are blended at a weight ratio of 93.5:0.7:4.8 and added to the reactor. By solution polymerization, using dimethyl sulfoxide as a solvent, the temperature of the polymerization reaction is controlled at 60°C. The reaction time was 40 hours, and the PAN resin with a molecular weight of 180,000 and a molecular weight distribution of 2.5 was obtained by continuous polymerization. The weight content of PAN resin in the spinning dope is 18%.
[0064] 2. Filtration of spinning dope
[0065] The spinning dope is finely filtered through a 3μm filter material.
[0066] 3. The solidification of the spinning stock solution is spun by dry-jet wet spinning. After the fiber leaves the spinneret hole, it enters the first-stage coagulation bath. The temperature of the first-stage coagulation bath is 10°C. The content is 50wt%, and the coagulation time is 1.5min. After the coagulated filam...
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