Manufacturing method for 48K polyacrylonitrile-based carbon fiber precursor
A technology of polyacrylonitrile-based carbon fiber and manufacturing method, which is applied in the field of manufacturing 48K polyacrylonitrile carbon fiber precursors, can solve the problems of increased viscosity of the system, slow heat exchange rate, and low yield, and achieve narrow molecular weight distribution. Fast heat rate, less damage effect
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[0023] According to the present invention, the preparation method of the polymer powder for the polyacrylonitrile-based carbon fiber precursor preferably includes:
[0024] Add acrylonitrile monomer, second monomer, itaconic acid, initiator and deionized water into the polymerization tank, and react at 55-65°C and 100-130rpm for 4-6h under stirring, and the obtained product is desingled, washed, After drying, the polymer powder for polyacrylonitrile-based carbon fiber precursors is obtained.
[0025] According to the present invention, the second monomer is preferably acrylic acid, methacrylic acid, methyl acrylate, acrylamide or methyl methacrylate. The initiator is preferably ammonium persulfate-ammonium sulfite or ammonium persulfate-ammonium bisulfite, the number of ammonium persulfate is preferably 0.1-1.0 parts, and the number of ammonium sulfite or ammonium bisulfite is preferably 0.1-0.75 parts .
[0026] According to the present invention, the weight and number rati...
Embodiment 1
[0031] The acrylonitrile monomer solution is passed through a metering pump according to the ratio of 50% (Wt%), the second monomer methyl acrylate 5% (Wt%), and the third monomer itaconic acid 1.5% (Wt%) is added to the polymerization tank, Add ammonium persulfate and ammonium bisulfite according to the ratio of 0.15% (Wt%) and 0.70% (Wt%) and deionized water 42.65% (Wt%) into the polymerization kettle respectively, keep the temperature at 60°C, and the reaction time is 4 hours , with a stirring rate of 120rpm, the obtained slurry containing acrylonitrile powder is continuously discharged from the polymerization tank, and polymer powder for polyacrylonitrile-based carbon fiber precursors is obtained after single removal, washing and drying. After testing, the weight-average molecular weight of the polymer was 187,000, and the molecular weight distribution index was 2.56.
[0032] Mix the polymer powder for polyacrylonitrile-based carbon fiber precursor obtained above with DMA...
Embodiment 2
[0035] The acrylonitrile monomer solution is according to the ratio of 40% (Wt%) by metering pump, the second monomer acrylic acid 5% (Wt%), the third monomer itaconic acid 4% (Wt%) is added to the polymerization tank, and the Ammonium sulfate and ammonium bisulfite are added in the polymerization kettle according to the ratio of 0.10% (Wt%) and 0.75% (Wt%) and deionized water 50.15% (Wt%) respectively, and the temperature is kept at 65 ° C, and the reaction time is 4 hours. Stir The speed is 120rpm, and the obtained slurry containing acrylonitrile powder is continuously discharged from the polymerization tank, and the polymer powder for polyacrylonitrile-based carbon fiber precursors is obtained after single removal, washing and drying. After testing, the weight average molecular weight of the polymer was 239,000, and the molecular weight distribution index was 2.59.
[0036] Mix the polymer powder for polyacrylonitrile-based carbon fiber precursor obtained above with DMAC at...
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