Method for preparing polyacrylonitrile-based carbon fiber precursors without skin-core structure
A polyacrylonitrile-based carbon fiber and polyacrylonitrile spinning technology, which is applied in the field of carbon fiber precursors, can solve the problems of unfavorable precursor comprehensive performance, reduced production costs, and increased holes in the precursors, achieving fewer defects and higher draw ratios The effect of improving and improving production efficiency
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Embodiment 1
[0033] Add 21% (mass percentage based on the sum of the three substances) of polystyrene with a viscosity-average molecular weight of 78,000 in the dimethyl sulfoxide / water mixed solvent of 5% (based on the percentage of total mass of dimethyl sulfoxide and water) containing water. Acrylonitrile resin, stirred at a constant speed at 50°C for 3 hours to disperse and swell, stirred at 70°C for 5 hours to fully dissolve, then stood at 70°C for defoaming, and placed in a dry environment at 25°C Mature at a medium constant temperature for 3 hours, extrude through a spinneret on a twin-screw extruder, pass through a 3cm air section, and then enter a methanol extraction bath at a temperature of 25°C to solidify and form, and control the winding speed of the winding roller and the extrusion speed of the stock solution The ratio is 10. The as-spun filaments were washed and stretched 1.5 times in a water bath at 40°C, stretched 2 times and 2.5 times in hot water at 80°C and 95°C in turn...
Embodiment 2
[0035] In the dimethylacetamide / water mixed solvent of 1% (based on the percentage of total mass of dimethylacetamide and water) containing water, add 23% (based on the mass percentage of the sum of the three substances) of polystyrene with a viscosity-average molecular weight of 78000 Acrylonitrile resin, stirred at a constant speed at 50°C for 3 hours to disperse and swell, stirred at 75°C for 5 hours to fully dissolve, then stood at 75°C for defoaming, and placed in a dry environment at 25°C Mature at a medium constant temperature for 2 hours, extrude through the spinneret on the twin-screw extruder, pass through a 3cm air section, and then enter the methanol extraction bath with a temperature of 25°C to solidify and form, and control the winding speed of the winding roller and the extrusion speed of the stock solution The ratio is 10. The as-spun filaments were washed and stretched 1.5 times in a water bath at 40°C, stretched 2 times and 2.5 times in hot water at 80°C and ...
Embodiment 3
[0037]Add 23% (mass percentage based on the sum of the three substances) of polystyrene with a viscosity-average molecular weight of 78,000 in the dimethyl sulfoxide / water mixed solvent of 5% (based on the percentage of total mass of dimethyl sulfoxide and water) containing water. Acrylonitrile resin, stirred at a constant speed at 50°C for 3 hours to disperse and swell, stirred at 80°C for 5 hours to fully dissolve, then stood at 80°C for defoaming, and placed in a dry environment at 25°C Mature at a medium constant temperature for 2 hours, extrude through a spinneret on a twin-screw extruder, pass through a 3cm air section, and enter a methanol / ethanol extraction bath with a temperature of 20°C and a methanol content of 80% by mass to solidify and form. The ratio of the winding speed of the winding roll to the dope extrusion speed is 12. The as-spun filaments were washed and stretched 1.8 times in a water bath at 40°C, stretched 2 times and 2.5 times in hot water at 85°C and...
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