Method for preparing high-strength polyacrylonitrile-based precursor for carbon fiber
A polyacrylonitrile-based carbon fiber and acrylonitrile technology, which is applied in spinning solution preparation, fiber treatment, wet spinning, etc., can solve the problem of insufficient high-performance carbon fiber, and achieve low production cost of raw silk, small fineness, wool little effect
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[0034] A method for preparing high-strength polyacrylonitrile-based precursors for carbon fibers, the specific steps are as follows: (wherein the percentage concentration is mass ratio percentage)
[0035] 1) Using acrylonitrile and itaconic acid as comonomers, using azobisisobutyronitrile to initiate homogeneous solution polymerization of acrylonitrile and comonomers in dimethyl sulfoxide (DMSO) to obtain spinning dope, control The temperature of the spinning stock solution is 40-70°C, and the solid content is 18-24%;
[0036] 2) The raw liquid after polymerization is separated under the pressure of -60~-78KPa, and then treated by 3um primary filtration.
[0037] 3) The stock solution after primary filtration is degassed under the pressure of -78~-100KPa, and then sent to the spinning unit through secondary filtration of 1um.
[0038]4) The refined spinning stock solution is extruded from the spinneret through the metering pump and the three-stage filter of 0.5um into the fi...
Embodiment 1
[0054] It is composed of 99% (wt) acrylonitrile and 1% (wt) itaconic acid, and the solid content is 20.5% (wt) in a dimethyl sulfoxide solution for solution polymerization to obtain a polymer with an intrinsic viscosity of [ η] was 1.78.
[0055] The polymer is singled out under the pressure of -76KPa through the single removal tank, and then undergoes a 3um level primary filtration treatment. Then, after degassing treatment in a defoaming tank with a pressure of -97KPa, it is sent to a 1um-level secondary filtration system, and the stock solution after refining treatment is transported to the spinning unit, and the temperature of the stock solution is controlled at 55°C.
[0056] The spinning stock solution is extruded from the spinneret to the coagulation bath through a 0.5um candle wick filter. The total number of holes in the spinneret is 12000, the hole diameter is 0.07mm, and the hole length is 0.25mm.
[0057] The coagulation liquid in the coagulation bath is made up ...
Embodiment 2
[0063] Change the drawing speed of the pulling roll outside the coagulation bath in embodiment 1 to 4m / min, reduce the draw ratio of pre-drawing simultaneously, make the total draw ratio of fiber in the whole operation be about 12 times, except this In addition, using the same apparatus and method as in Example 1, polyacrylonitrile-based carbon fiber precursors were produced.
[0064] The fineness of the monofilament in the obtained fiber bundle is 0.67dtex, the monofilament strength is 8.7cN / dtex, the elongation is 10.4%, and the density is 1.181g / cm3, there is a small amount of "waist type" in the fiber bundle section, and the fiber silicone oil content was 0.78%.
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