Method for preparing high-strength polyacrylonitrile-based precursor for carbon fiber
A technology of polyacrylonitrile-based carbon fiber and acrylonitrile, which is applied in the direction of 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, and high production process compact effect
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[0033] A method for preparing high-strength polyacrylonitrile-based precursor for carbon fiber, the specific steps are as follows: (wherein the percentage concentration is the mass ratio percentage)
[0034] 1) With 99wt% of acrylonitrile and 1wt% of itaconic acid as comonomers, azobisisobutyronitrile was used to initiate homogeneous solution polymerization of acrylonitrile and comonomers in DMSO (DMSO). Obtain spinning dope, and control the temperature of the spinning dope to 40~70℃ and the solid content of 18~24%;
[0035] 2) The raw solution after polymerization is stripped under a pressure of -60 ~ -78KPa, and then subjected to a 3um primary filtration treatment.
[0036] 3) The stock solution after the primary filtration is subjected to defoaming treatment under a pressure of -78~-100KPa, and then sent to the spinning unit through a secondary filtration of 1um.
[0037] 4) The refined spinning dope is extruded from the spinneret into the first coagulation bath through a metering ...
Embodiment 1
[0053] It is composed of 99% (wt) of acrylonitrile, 1% (wt) of itaconic acid, and the solid content of 20.5% (wt) of dimethyl sulfoxide solution for solution polymerization to obtain a polymer with intrinsic viscosity [ η] is 1.78.
[0054] The polymer is removed from the single reactor at a pressure of -76KPa, and then subjected to a 3um level primary filtration treatment. Then, after defoaming treatment in a defoaming tank with a pressure of -97KPa, it is sent to a 1um second
[0055] Grade filtration system, the stock solution after the refining treatment is transported to the spinning unit, and the stock solution temperature is controlled to 55°C.
[0056] The spinning dope passes through a 0.5um candle wick filter and is extruded from the spinneret to the coagulation bath. 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 composed of 70% (wt) DMSO and 30% (w...
Embodiment 2
[0063] The traction speed of the traction roller outside the coagulation bath in Example 1 was changed to 4m / min, and the draft ratio of the pre-draft was reduced, so that the total draft ratio of the fiber in the whole process was about 12 times. In addition, the same apparatus and method as in Example 1 were used to produce polyacrylonitrile-based carbon fiber precursors.
[0064] The monofilament in the obtained fiber bundle has a fineness of 0.67dtex, a monofilament strength of 8.7cN / dtex, an elongation of 10.4%, a density of 1.181g / cm3, a small amount of "waist type" in the cross section of the fiber bundle, and fiber silicone oil content It is 0.78%.
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