A kind of wet spinning method of polyacrylonitrile fiber and polyacrylonitrile fiber
A polyacrylonitrile fiber, wet spinning technology, applied in wet spinning, fiber chemical characteristics, single-component synthetic polymer rayon, etc. It can solve problems such as poor spinnability, low equipment requirements, and reduce fiber defects.
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Embodiment 1
[0069] Preparation of spinning solution: adopt initiator azobisisobutyronitrile to make main monomer acrylonitrile and comonomer vinylidene chloride carry out polymerization reaction in solvent dimethyl sulfoxide (wherein, acrylonitrile accounts for 1% of the total monomer mass 60%, vinylidene chloride accounts for 40% of the total monomer mass, the initiator consumption is 0.8% of the total monomer mass, the solvent consumption accounts for 70% of the polymerization system quality (that is, the total mass of reactants), and the polymerization reaction temperature is 70°C , reaction time 20h), to obtain a polymerization liquid; after the polymerization liquid is de-singled and defoamed, a spinning liquid is obtained. Wherein, the polymerization conversion rate is 96.2%, the solid content of the spinning solution is 30%, and the use temperature of the spinning solution is 60° C., and the spinning solution is spun.
[0070] Spinning: Wet spinning is adopted, and the diameter of ...
Embodiment 2
[0079] Preparation of spinning solution: use initiator azobisisobutyronitrile to make main monomer acrylonitrile and comonomer dibromoethylene carry out polymerization reaction in solvent dimethyl sulfoxide (wherein, acrylonitrile accounts for 1% of the total monomer mass 55%, dibromoethylene accounted for 45% of the total monomer mass, the initiator consumption was 0.8% of the total monomer mass, the solvent consumption accounted for 65% of the polymerization system quality, the polymerization reaction temperature was 65°C, and the reaction time was 16h), and the polymerization obtained liquid; after the polymerization liquid is de-singled and defoamed, the spinning liquid is obtained. Wherein, the polymerization conversion rate is 93.5%, the solid content of the spinning solution is 35%, and the use temperature of the spinning solution is 50° C., and the spinning solution is spun.
[0080] Spinning: Wet spinning is adopted, and the diameter of the spinneret hole is 0.075mm. ...
Embodiment 3
[0089]Preparation of spinning solution: use initiator azobisisobutyronitrile to make main monomer acrylonitrile and comonomer vinylidene chloride carry out polymerization reaction in solvent dimethylacetamide (wherein, acrylonitrile accounts for 1% of the total monomer mass 60%, vinylidene chloride accounts for 40% of the total monomer mass, the initiator consumption is 0.8% of the total monomer mass, the solvent consumption accounts for 60% of the polymerization system quality, the polymerization reaction temperature is 65 ° C, and the reaction time is 20h), and the polymerization liquid; after the polymerization liquid is de-singled and defoamed, the spinning liquid is obtained. Wherein, the polymerization conversion rate is 91.8%, the solid content of the spinning solution is 40%, and the use temperature of the spinning solution is 30° C., and the spinning solution is spun.
[0090] Spinning: Wet spinning is adopted, and the diameter of the spinneret hole is 0.1mm.
[0091...
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Abstract
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