Oiling method of polyacrylonitrile-based carbon fiber precursor
A polyacrylonitrile-based carbon fiber and polyacrylonitrile technology, which is used in filament generation, rayon cleaning/drying, textiles and papermaking, etc. The oil is uniform and the effect of reducing oil sticking to the roller
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Embodiment 1
[0025] 1. Preparation of stock solution: Distilled acrylonitrile (AN) and itaconic acid (IA) in a ratio of 97:3, with a solid content of 20%, and azobisisobutyronitrile (AIBN) accounts for 0.4wt% of the comonomer, Add dimethyl sulfoxide (DMSO) as a solvent into the reactor, and react at a constant temperature of 59° C. for 20 hours under the protection of nitrogen to obtain a binary acrylonitrile copolymer spinning solution. Then the spinning solution is decompressed to remove residual monomers and air bubbles, and then filtered through a 5 μm filter material to obtain an acrylonitrile copolymer spinning solution. After testing, the molecular weight is 80021, the molecular weight distribution is 3.34, and the viscosity is 75 Pa·s at 60°C.
[0026] 2. Coagulation forming: The spinning dope is metered by a metering pump, filtered again at 3 μm, extruded through a spinneret and then enters the first coagulation bath. The temperature of the coagulation bath is 20°C, the concentrat...
Embodiment 2
[0034]The polyacrylonitrile raw silk from water washing enters the first oiling process, the oiling concentration of the first oiling process is 1.5%, and the temperature is normal temperature. 75°C, the time is 40s, after drying, the raw silk is soaked and extruded in a water bath, the temperature of pure water is 40°C, and the soaking time is 5s, by adjusting the pressure between the extrusion roller and the oiling bath roller Control the moisture content of the raw silk to 10%, and then carry out the second oiling, the concentration of the second oiling is 3%, the temperature is normal temperature, the raw silk leaving the second oiling is squeezed, and then enters the second drying and densification. The temperature is 120°C, the time is 40s, the oiling rate of the polyacrylonitrile precursor is 1.2%, and the oiling rate difference between the outer and middle of the polyacrylonitrile precursor tow is 0.08%; The oil rate difference is 0.2%, the polyacrylonitrile raw silk i...
Embodiment 3
[0036] The polyacrylonitrile raw silk from washing enters the first oiling process, the oiling concentration of the first oiling process is 2.5%, and the temperature is normal temperature. 85°C, the time is 20s, after drying, the raw silk is soaked in a water bath and squeezed, the pure water temperature is 35°C, the soaking time is 10s, the moisture content of the raw silk is controlled at 16%, and then the second oiling is carried out. The second oiling concentration is 3%, the temperature is normal temperature, the raw silk leaving the second oiling is squeezed, and then enters the second drying and densification, the temperature is 110°C, the time is 50s, and the polyacrylonitrile raw silk is oiled The rate is 1.1%, and the difference in oiling rate between the outside and the middle of the polyacrylonitrile precursor tow is 0.05%; There is no color difference, and the adhesion of the oil agent on the surface of the second drying and densifying roller is not obvious. After...
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