Preparation method of polyacrylonitrile-based carbon fiber
A polyacrylonitrile-based carbon fiber, polyacrylonitrile technology, applied in the chemical characteristics of fibers, textiles and papermaking, etc., can solve the problems of carbon fiber carbonization yield and mechanical properties decline, defects affecting carbon fiber performance, excessive molecular chain breakage and other problems. Improve the oiling rate and oiling uniformity, reduce the amount of coke discharge and the residue of silica, and prolong the life.
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Embodiment 1
[0027] The copolymer composition of the precursor is 95.5% acrylonitrile, 3.5% methyl acrylate, and 1% itaconic acid. After washing, the polyacrylonitrile raw silk enters the first oiling and extrusion rollers, and then enters the first drying and densification at a temperature of 70°C for 20s; After that, the moisture content of the raw silk is controlled to 5% by adjusting the pressure between the extrusion roller and the oiling and bathing roller, and then the second oiling is carried out, and the polyacrylonitrile raw silk leaving the second oiling is extruded again. , enter the second drying and densification, the temperature is 100 ℃, the time is 20s; finally, after steam drawing and heat setting, the steam pressure of steam drawing is 3 kg, and the drafting ratio is 2.5; the steam pressure of heat setting is 1 kg, and the drawing The draw ratio was 0.96, and a polyacrylonitrile precursor was obtained. The polyacrylonitrile fiber was thermally stabilized in the range of...
Embodiment 2
[0029] The copolymer composition of the precursor is 96.0% acrylonitrile, 3.5% methyl acrylate, and 0.5% acrylamide. After washing, the polyacrylonitrile raw silk enters the first oiling and squeezing rollers, and then enters the first drying and densification at a temperature of 100 °C and a time of 60s; After that, the moisture content of the raw silk is controlled to 10% by adjusting the pressure between the extrusion roller and the oiling and bathing roller, and then the second oiling is carried out, and the polyacrylonitrile raw silk leaving the second oiling is extruded again. , enter the second drying and densification, the temperature is 140 ℃, the time is 60s; finally, after steam drawing and heat setting, the steam pressure of steam drawing is 2.5 kg, the drafting ratio is 2.2; the steam pressure of heat setting is 1.2 kg, the drawing The draw ratio was 0.95, and a polyacrylonitrile precursor was obtained. The polyacrylonitrile precursor was thermally stabilized in ...
Embodiment 3
[0031]The copolymer composition of the precursor is 97.0% acrylonitrile and 3.0% acrylamide respectively. After washing, the polyacrylonitrile raw silk enters the first oiling and squeezing rollers, and then enters the first drying and densification at a temperature of 100 °C and a time of 60s; After that, the moisture content of the raw silk is controlled to 20% by adjusting the pressure between the extrusion roller and the oiling and bathing roller, and then the second oiling is carried out, and the polyacrylonitrile raw silk leaving the second oiling is extruded again. , enter the second drying and densification, the temperature is 140 ℃, the time is 60s; finally, after steam drawing and heat setting, the steam pressure of steam drawing is 3.5 kg, and the drafting ratio is 2.7; The draw ratio was 0.97, and a polyacrylonitrile precursor was obtained. Through 5 air atmosphere heating furnaces, the polyacrylonitrile raw silk is thermally stabilized in the range of 180 ~ 280 °...
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