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A kind of drawing method of polyacrylonitrile fiber

A technology of polyacrylonitrile fiber and polyacrylonitrile, which is applied in the direction of stretch spinning, fiber chemical characteristics, wet spinning, etc., and can solve the problem of high temperature and high pressure resistance of equipment, affecting fiber mechanics, thermal performance, solvents, etc. Remove problems such as limited effect, achieve good quality, low cost, and complete removal effect

Inactive Publication Date: 2015-10-21
DONGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In the method disclosed in the above-mentioned method, one or more washing tanks are required for water washing stretching or spray washing, which requires a large amount of water to remove a small amount of solvent in the fiber, and produces a large amount of waste liquid containing spinning solvent, and after After multiple washings, the removal effect of the solvent in the fiber is limited, and there is still a small amount of solvent remaining, which affects the mechanical and thermal properties of the fiber, and then affects the quality of the fiber; and the use of atmospheric pressure water vapor to remove the solvent, the solvent removal effect is better than that of a large amount of water. The effect is good, but because it is removed in atmospheric pressure steam, no stretching is applied during the process to increase the removal efficiency, and there is still a small amount of solvent remaining in the fiber
[0005] The high-stretching of the PAN fiber of the carbon fiber precursor is realized in the steam stretching process section. Usually, the steam stretching needs to be carried out under a certain temperature and pressure. The existing steam stretching usually requires a steam pressure of 0.6 MPa or more. Therefore, It is required that the steam stretching device has higher sealing performance, and the patent of publication number CN101235568A discloses a steam pressure sealing device, and a high-temperature gas sealing chamber with the same pressure as that of the steam stretching chamber is used at both ends of the steam stretching chamber Connected to ensure the temperature and pressure in the water vapor stretching chamber to achieve the purpose of high-stretching polyacrylonitrile fibers. The utility model patent No. 02247164.2 uses a steam chamber outside the steam chamber to increase the steam temperature and pressure and The sealing of the device, these methods are to further modify the steam stretching device to improve the sealing of the stretching device. Although this improves the stretching effect to a certain extent, the workload and cost are high for the modification of the device. High temperature and high pressure resistance is required for equipment, and a large amount of energy is required to achieve high vapor pressure

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Set the viscosity average molecular weight to 2×10 4 Polyacrylonitrile (acrylonitrile homopolymer) was dissolved in N,N-dimethylformamide to obtain a spinning solution with a concentration of 18wt%.

[0030] The spinning solution at a temperature of 70°C is extruded into a coagulation bath at 35°C through a metering pump and a spinneret. The composition of the coagulation bath is 60wt% N,N-dimethylformamide, 40wt% deionized water, and guided The roller enters the first stretching bath composed of 60°C deionized water and the second stretching bath composed of 75°C deionized water successively, and after stretching in two water baths, the composition is 95wt% polyacrylonitrile, 3wt% % N,N-dimethylformamide and polyacrylonitrile filament with the balance water.

[0031] The polyacrylonitrile filament stretched in the second water bath is subjected to two-stage steam stretching. The pressure in the first stage of steam stretching is 0.15±0.01MPa, the stretching ratio is 2 times...

Embodiment 2

[0033] Set the viscosity average molecular weight to 3×10 4 Polyacrylonitrile (acrylonitrile homopolymer) was dissolved in N,N-dimethylacetamide to obtain a spinning solution with a concentration of 18wt%.

[0034] The spinning solution at a temperature of 70°C is extruded into a coagulation bath at 35°C through a metering pump and a spinneret. The composition of the coagulation bath is 60wt% N,N-dimethylacetamide, 40wt% deionized water, and guided The roll enters the first stretching bath composed of 60°C deionized water and the second stretching bath composed of 75°C deionized water, and the third stretching bath composed of 100°C deionized water is drawn through three water baths. After stretching, a polyacrylonitrile filament with a composition of 85% by weight of polyacrylonitrile, 10% by weight of N,N-dimethylacetamide and the balance of water is obtained.

[0035] The polyacrylonitrile filament stretched in three water baths is subjected to two-stage steam stretching. The pr...

Embodiment 3

[0037] Set the viscosity average molecular weight to 2.5×10 4 Polyacrylonitrile (acrylonitrile homopolymer) was dissolved in dimethyl sulfoxide to obtain a spinning solution with a concentration of 16wt%.

[0038] The spinning solution at a temperature of 65°C is extruded into a coagulation bath at 30°C through a metering pump and a spinneret. The composition of the coagulation bath is 50wt% dimethyl sulfoxide, 50wt% deionized water, and then enters 35 by the guide roller. The first stretching bath composed of deionized water at ℃ and the second stretching bath composed of deionized water at 90℃ are stretched by two water baths to obtain a composition of 80wt% polyacrylonitrile and 15wt% two Polyacrylonitrile filament with methyl sulfoxide and balance water.

[0039] The polyacrylonitrile filament stretched in the second water bath is subjected to three-stage steam stretching, the pressure in the first stage of steam stretching is 0.15±0.01MPa, the stretching ratio is 1.5 times, an...

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PUM

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Abstract

The invention relates to a polyacrylonitrile fiber stretching method which comprises the following steps: extruding a polyacrylonitrile spinning solution, moving into a coagulation bath for forming via or not via an air layer, moving into a stretching bath through a guide roller, and then performing multi-stage stretching on polyacrylonitrile fiber in saturated steam, wherein the polyacrylonitrile fiber comprises 30-95 wt% of polyacrylonitrile, 3-40 wt% of solvent and the balance of water; the steam pressure P1 of the saturated steam for first-stage steam stretching is kept at 0.11-0.15+ / -0.01 MPa, and the steam pressure PN for final-stage steam stretching is kept at 0.40-0.43+ / -0.01 MPa; and the multi-stage stretching is 2-7 stages, and the total stretching ratio is 3.0-29.7. The polyacrylonitrile fiber stretching method improves the orientation degree and the mechanical strength of macromolecular chains in the fiber, reduces the solvent residue in the fiber and enhances the performance of the fiber.

Description

Technical field [0001] The invention relates to a stretching method of polyacrylonitrile fiber, belonging to the field of polyacrylonitrile fiber preparation. Background technique [0002] Polyacrylonitrile fiber (PAN) is a synthetic fiber with excellent performance and an important fiber raw material for textile and industrial use. The industrialized spinning process of polyacrylonitrile fiber includes wet method, dry method and dry spray wet method. In the process of wet spinning and dry jet wet spinning, coagulation forming in a coagulation bath, washing and stretching in a water bath, washing with a large amount of water, drying and heat setting and other important process steps, are used in the production of high-quality special-purpose polyacrylonitrile fiber. In the preparation process, it is often necessary to perform high-temperature steam stretching on the dried fiber to improve the regularity and mechanical properties of the fiber structure. [0003] The publication nu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): D01D5/14D01D5/06D01F6/18
Inventor 殷学敏朱新军王华平张玉梅张历王彪杨春雷于金超
Owner DONGHUA UNIV