High-quality polyacrylonitrile spinning raw solution preparation method
A polyacrylonitrile spinning, high-quality technology, applied in the direction of spinning solution preparation, single-component synthetic polymer rayon, filament molding treatment, etc., can solve the problem of large CV value of carbon fiber precursor performance, carbon fiber spinning stock solution Solve the problems of low single removal efficiency and achieve the effect of improving the single removal efficiency, offsetting the volatilization of sulfoxide, and reducing the residual amount
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Embodiment 1
[0019] a. Preparation of stock solution: Distilled acrylonitrile (AN) and itaconic acid (IA) in a proportion of 98:2, solid content 20%, azobisisobutyronitrile (AIBN) accounted for 0.5wt% of the comonomer, Add dimethyl sulfoxide (DMSO) as a solvent to the reactor, and react under the protection of nitrogen at a constant temperature of 60°C for 20 hours to obtain a binary acrylonitrile copolymer spinning solution;
[0020] b. Raise the temperature of the single reactor to 60°C, evacuate the pressure of the single reactor to a vacuum of 30 mbar, and then slowly pump the prepared polymerization stock solution into the single reactor, and move from the bottom of the single reactor to The mixed gas of dimethyl sulfoxide and nitrogen is introduced into the kettle, the temperature of the mixed gas is 80℃, and the content of dimethyl sulfoxide is 40%. After the feeding is finished, the vacuum is maintained and the mixer gas is passed through until the residue is obtained. The unit amount...
Embodiment 2
[0024] a. Preparation of stock solution: Distilled acrylonitrile (AN) and itaconic acid (IA) in a ratio of 97:3, solid content 20%, azobisisobutyronitrile (AIBN) accounted for 0.4wt% of the comonomer, Add dimethyl sulfoxide (DMSO) as a solvent to the reactor, and react under the protection of nitrogen at a constant temperature of 60°C for 20 hours to obtain a binary acrylonitrile copolymer spinning solution;
[0025] b. Raise the temperature of the single-removing reactor to 50°C, then place the prepared polymerization stock solution in the single-removing reactor, and evacuate the pressure of the single-removing reactor to a vacuum degree of 50 mbar; The mixed gas of dimethyl sulfoxide and inert gas is passed into the mixture, the temperature of the mixed gas is 100 ℃, and the content of dimethyl sulfoxide is 80%. After the feeding is completed, the vacuum is maintained and the mixer gas is passed through until the residue is obtained. The unit amount is less than 0.3%;
[0026] ...
Embodiment 3
[0029] a. Preparation of stock solution: Distilled acrylonitrile (AN) and itaconic acid (IA) in proportion to 98:2, solid content 22%, azobisisobutyronitrile (AIBN) accounts for 0.5wt% of the comonomer, Add dimethyl sulfoxide (DMSO) as a solvent to the reactor, and react under the protection of nitrogen at a constant temperature of 60°C for 20 hours to obtain a binary acrylonitrile copolymer spinning solution;
[0030] b. Raise the temperature of the single reactor to 65°C, then place the prepared polymerization stock solution in the single reactor, and evacuate the pressure of the single reactor to a vacuum of 40mbar; and move from the bottom of the single reactor to the reactor The mixed gas of dimethyl sulfoxide and inert gas is introduced into the mixture. The temperature of the mixed gas is 110°C, and the content of dimethyl sulfoxide is 10%. After the feeding is completed, the vacuum is maintained and the mixer gas is introduced until the residue is obtained. The unit amoun...
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