Prepn. of polyacrylonitrile-base high-performance raw carbon fiber
A polyacrylonitrile-based, high-performance technology, which is applied in the field of preparation of polyacrylonitrile-based high-performance carbon fiber precursors, can solve problems such as increasing the concentration of the coagulation bath, the core-skin structure of the precursor, and the difficulty of large-scale drafting. Achieve the effects of avoiding uneven heating, small coefficient of variation of filaments, and reducing solvent content
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Embodiment 1
[0037] 1. Preparation of spinning dope
[0038] Acrylonitrile, itaconic acid, and methyl methacrylate are blended at a weight ratio of 96:1:3 and 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%.
[0039] 2. Filtration of silk stock solution
[0040] The spinning dope is finely filtered through a 5μm filter material.
[0041] 3. Solidification and molding of silk stock solution
[0042] Adopt dry spray wet spinning method spinning, after fiber leaves spinneret hole, enters the coagulation bath of the first stage, and the coagulation bath temperature of the first stage is 0 ℃, and the content of dimethyl sulfoxide in the coagulation bath is 45wt%, and coagulation...
Embodiment 2
[0061] 1. Preparation of silk stock solution
[0062] Acrylonitrile, itaconic acid, and methyl methacrylate are added to the reactor after being blended in a weight ratio of 92:2:6. By solution polymerization, using dimethyl sulfoxide as a solvent, the temperature of the polymerization reaction is controlled at 70 DEG C. The reaction time is 20 hours, continuous polymerization to obtain a PAN resin with a molecular weight of 200,000 and a molecular weight distribution of 3.0, and the weight content of the PAN resin in the silk stock solution is 23%.
[0063] 2. Filtration of spinning dope
[0064] The spinning dope is finely filtered through a 2.0μm filter material.
[0065] 3. Solidification and molding of the original solution
[0066] 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 65w...
Embodiment 3
[0086] 1. Preparation of spinning dope
[0087] Acrylonitrile, itaconic acid, and methyl methacrylate are added to the reactor after being blended at a weight ratio of 93.5: 0.7: 4.8. 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%.
[0088] 2. Filtration of spinning dope
[0089] The spinning dope is finely filtered through a 3μm filter material.
[0090] 3. Solidification and molding of spinning dope
[0091] Adopt dry-jet wet-spinning method spinning, after fiber leaves spinneret orifice, enters first stage coagulation bath, and first stage coagulation bath temperature is 10 ℃, and the content of dimethyl sulfoxide in the coagulation bath is 50wt%, coagula...
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