Spinning method of high molecular weight and high viscosity spinning solution
A spinning solution, high molecular weight technology, applied in wet spinning, stretch spinning, single-component synthetic polymer rayon, etc., can solve the problems of high fiber breakage rate and poor fiber formation, and achieve uniform color , low CV value and stable performance
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Embodiment 1
[0026] (1) Preparation of spinning stock solution: add acrylonitrile, itaconic acid and methyl methacrylate to the polymerization kettle, then add initiator and dimethyl sulfoxide, react at a temperature of 40° C. for 10 hours, and then Remove the unreacted monomer and the bubbles generated by the reaction to obtain the spinning dope, the initiator is azobisisoheptanonitrile, the mass ratio of acrylonitrile and comonomer is 98.5:1.5, and the initiator accounts for the mass of the total monomer The percentage is 0.08%, and the total monomer concentration is 15%. After filtration, the high-performance polyacrylonitrile copolymer spinning stock solution is obtained. The spinning stock solution has a subweight of 110,000, a molecular weight distribution of 2.0, and a viscosity of 90Pa at 60°C. S, the temperature of the spinning dope is 60°C.
[0027](2) Coagulation forming: the present invention adopts the method of wet spinning to prepare, and the spinning dope is metered by a me...
Embodiment 2
[0033] (1) Preparation of spinning stock solution: Add acrylonitrile, ammonium itaconate and methacrylic acid to the polymerization kettle, then add initiator and dimethyl sulfoxide, react at a temperature of 60°C for 24 hours, and then remove Remove the unreacted monomer and the bubbles generated by the reaction to obtain the spinning dope, the initiator is azobisisobutyronitrile, the mass ratio of acrylonitrile and comonomer is 90:10, and the initiator accounts for the mass percentage of the total monomer is 0.25%, and the total monomer concentration is 25%. After filtration, a high-performance polyacrylonitrile copolymer spinning stock solution is obtained. The spinning stock solution has a seed weight of 290,000, a molecular weight distribution of 1.8, and a viscosity of 270Pa·S at 60°C. , The spinning dope temperature is 60°C.
[0034] (2) Coagulation forming: the present invention adopts the method of wet spinning to prepare, and the spinning dope is metered by a meterin...
Embodiment 3
[0040] (1) Preparation of spinning stock solution: Add acrylonitrile and itaconic acid to the polymerization kettle, then add initiator and dimethyl sulfoxide, react at a temperature of 65°C for 30 hours, and then remove unreacted mono body and the bubbles generated by the reaction to obtain the spinning dope, the initiator is azobisisobutyronitrile, the mass ratio of acrylonitrile and comonomer is 95:5, and the mass percentage of the initiator in the total monomer is 0.2%, and the total The concentration of the monomer is 20%, and the high-performance polyacrylonitrile copolymer spinning stock solution is obtained through filtration. The spinning stock solution has a subweight of 150,000, a molecular weight distribution of 15, a viscosity of 146Pa·S at 60°C, and a spinning stock solution temperature of is 60°C.
[0041] (2) Coagulation forming: the present invention adopts the method of wet spinning to prepare, and the spinning dope is metered by a metering pump, and after fi...
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