Polyacrylonitrile fibers and wet spinning method thereof
A polyacrylonitrile fiber, wet spinning technology, applied in the direction of wet spinning, fiber chemical characteristics, single-component synthetic polymer rayon, etc., can solve the problem of the decline in the mechanical properties of polyacrylonitrile fibers, and the spinning process can be spun problems such as poor spinnability, to achieve the effect of solving poor spinnability, low equipment requirements, and reducing fiber defects
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2019-07-26
Abstract
Description
technical field
[0001] The invention relates to the technical field of polyacrylonitrile fibers, in particular to a wet spinning method of polyacrylonitrile fibers and polyacrylonitrile fibers. Background technique
[0002] Polyacrylonitrile fiber is one of the three major synthetic fibers in the world. It has the advantages of good elasticity, soft hand feeling and good warmth retention. It is known as "synthetic wool", so it is widely used in clothing, decoration, outdoor textiles and other fields. However, the limiting oxygen index LOI value of polyacrylonitrile fiber is only 17-18.5%. It is one of the most flammable synthetic fibers, and it is easy to cause fire and threaten people's life and property safety during use. Therefore, flame-retardant polyacrylonitrile fiber has also become a development and research hotspot in the synthetic fiber industry of various countries.
[0003] Because the polymer chemical modification method has the advantages of less amount of fla...
Examples
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...