Preparation method and polymerization equipment of acrylonitrile base carbon fiber spinning solution
An acrylonitrile-based carbon fiber and polymerization reaction technology, which is applied in the fields of fiber chemical characteristics, textiles and papermaking, can solve the problems of material properties and structure inhomogeneity, and achieve good mixing effect, uniform chemical structure and improved reaction degree.
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Embodiment 1
[0026] Embodiment 1: Weigh 20Kg of dimethyl sulfoxide, 6.336Kg of acrylonitrile, 132g of acrylamide and 66g of itaconic acid, pour them into a 50L reaction kettle in turn, stir and dissolve completely, and bubbling argon for 20min to remove the solution and Air in the kettle, and hot water at 50°C is passed through the jacket of the reactor. When the material temperature is 50°C, 36.3g of azobisisoheptanenitrile is added, and the reaction starts. After 30 minutes, the twin-screw reaction extruder is turned on to circulate the material. The output of the extruder is 50Kg / h, and the temperature of the extruder jacket is kept at 50 °C. At the same time, 3.4 kg of dimethyl sulfoxide and 66 g of itaconic acid were added to the feeding tank of the extruder, and the feeding was completed within 3 hours with a metering pump. Discharge after 15h of polymerization. The conversion rate was 92.6%, the weight-average molecular weight was 158,000, and the molecular weight distribution coe...
Embodiment 2
[0027] Embodiment 2: Weigh 20Kg of dimethyl sulfoxide, 6.336kg of acrylonitrile, 132g of acrylamide and 66g of itaconic acid, pour them into a 50L reactor successively, and after stirring and dissolving completely, bubbling argon for 20min to remove the solution and Air in the kettle, and hot water at 45°C is passed through the jacket of the reactor. When the temperature of the material is 50°C, 46.2g of azobisisoheptanenitrile is added, and the reaction starts. After 30 minutes, two twin-screw reaction extruders connected in series are turned on to circulate the material. The output of the extruder is 50Kg / h, and the extruder is kept The jacket temperature was 45°C. At the same time, 3.4 kg of dimethyl sulfoxide and 66 g of itaconic acid were added to the feeding tank of the extruder, and the feeding was completed within 3 hours with a metering pump. Discharge after 20h of polymerization. The conversion rate was 95.1%, the weight average molecular weight was 135,000, and th...
Embodiment 3
[0028] Embodiment 3: Weigh 17.5Kg of dimethyl sulfoxide, 4.85kg of acrylonitrile, 75g of methyl acrylate and 30g of itaconic acid, pour them into a 50L reactor successively, and after stirring and dissolving completely, 20min of argon bubbling to remove The solution and the air in the kettle, and at the same time, the jacket of the reactor is passed through hot water at 60°C. When the material temperature is 60 ℃, add 30.0g of azobisisobutyronitrile, and the reaction starts. After 30 minutes, open two twin-screw reaction extruders in series to circulate the material. The output of the extruder is 50Kg / h. Keep the extruder The jacket temperature was 60°C. At the same time, 2.5 kg of dimethyl sulfoxide and 35 g of itaconic acid were added to the feeding tank of the extruder, and the feeding was completed within 4 hours with a metering pump. Discharge after 12h of polymerization. The conversion rate was 91.6%, the weight-average molecular weight was 132,000, and the molecular w...
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