Preparation method of graphene/polyacrylonitrile spinning solution
A technology of polyacrylonitrile spinning and graphene, applied in the direction of conductive/antistatic filament manufacturing, rayon manufacturing, one-component synthetic polymer rayon, etc.
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Embodiment 1
[0029] The polymerization adopts a two-step aqueous phase suspension polymerization process, with acrylonitrile (AN) as the first monomer, methyl acrylate (MA) as the second monomer, and sodium methacrylate (A1) as the third monomer. Sodium chlorate (A2) and sodium metabisulfite (A3) are initiators, β-hydroxyethanethiol (A4) is a molecular weight regulator, and pure water is a reaction medium. After polymerization, termination, single removal, and water washing, the polymer sludge is prepared. The slurry is stored in storage tanks.
[0030] The ratio of the feed quality of AN and MA is 91.4:8.6; The ratio of each material feed flow is: the mass concentration of the first monomer and the second monomer is 34%, the A1 / M mass ratio is 0.23%, A2 / The mass ratio of M is 0.50%, the molar ratio of A3 / A2 is 1.5, the mass ratio of A4 / M is 0.22%, and the quality of pure water accounts for 65% of the total mass of the solution; the volume of the polymerization tank is 8.3m 3 , the react...
Embodiment 2
[0038] The polymerization adopts a two-step aqueous phase suspension polymerization process, with acrylonitrile (AN) as the first monomer, vinyl acetate (VAC) as the second monomer, and sodium methacrylate (A1) as the third monomer. Sodium chlorate (A2) and sodium metabisulfite (A3) are initiators, β-hydroxyethanethiol (A4) is a molecular weight regulator, and pure water is a reaction medium. After polymerization, termination, single removal, and water washing, the polymer sludge is prepared. The slurry is stored in storage tanks.
[0039] The feed mass ratio of AN and VAC is 89.5:10.5. The ratio of each material feed flow rate is: the mass concentration of monomer (AN and MA) is 34%, the A1 / M mass ratio is 0.23%, the A2 / M mass ratio is 0.50%, the A3 / A2 molar ratio is 1.5, and the A4 The mass ratio of / M is 0.22%, and the quality of pure water accounts for 65% of the total mass of the solution; the volume of the polymerization tank is 8.3m 3 , the reaction time was 53min, th...
Embodiment 3
[0043] The polymerization adopts a two-step aqueous phase suspension polymerization process, with acrylonitrile (AN) as the first monomer, methyl acrylate (MA) as the second monomer, and sodium methacrylate (A1) as the third monomer. Sodium chlorate (A2) and sodium metabisulfite (A3) are initiators, β-hydroxyethanethiol (A4) is a molecular weight regulator, and pure water is a reaction medium. After polymerization, termination, single removal, and water washing, the polymer sludge is prepared. The slurry is stored in storage tanks.
[0044] The feed mass ratio of AN and MA was 90:10. The ratio of each material feed flow is: the mass concentration of monomer (AN and MA) is 30%, and A1 / M mass ratio is 0.2%, and A2 / M mass ratio is 0.40%, and A3 / A2 mol ratio is=1, The mass ratio of A4 / M is 0.2%, and the pure water mass accounts for 69% of the total mass of the solution; the volume of the polymerization tank is 8.3m 3 , the reaction time is 52min, the reaction temperature is 55°C...
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