High-elongation special-shaped polyamide fiber 66 and production method thereof
A production method and technology of nylon, applied in the direction of stretch spinning, fiber processing, filament/thread forming, etc., can solve the problems of dependence on imports, complex production technology, etc., to improve quality, process stability, and improve spinnability. Effect
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Embodiment 1
[0032] A production method of high-elongation special-shaped nylon 66 fiber, comprising the following steps:
[0033] (1) Melt polymerization:
[0034] a. Transport the nylon 66 salt solution to the concentration tank and heat it to 130°C for concentration, concentrate the nylon 66 salt solution with a mass percentage of 50% to 70%, and discharge a large amount of water vapor;
[0035] b. The nylon 66 salt solution concentrated in step a is transported to the reactor (the reaction temperature is controlled at 255-268°C, the reaction time is controlled at 2.5~3.0h, and the reaction pressure is 1.85±0.5MPa) for high-pressure dehydration and polycondensation to form prepolymer then sent to the flash evaporator, the pressure of the material is reduced from 1.85MPa to normal pressure after passing through the multi-section different-diameter material pipe, and the vapor-liquid mixed polymer is generated;
[0036] c. The vapor-liquid mixed polymer obtained in step b is subjected...
Embodiment 2
[0049] A production method of high-elongation special-shaped nylon 66 fiber, comprising the following steps:
[0050] (1) Melt polymerization:
[0051] a. Transport the nylon 66 salt solution to the concentration tank and heat it to 134°C for concentration, concentrate the nylon 66 salt solution with a mass percentage of 55% to 74%, and discharge a large amount of water vapor;
[0052] b. The nylon 66 salt solution concentrated in step a is transported to the reactor (the reaction temperature is controlled at 255-268°C, the reaction time is controlled at 2.5~3.0h, and the reaction pressure is 1.85±0.5MPa) for high-pressure dehydration and polycondensation to form prepolymer The material is then sent to the flash evaporator, and the pressure of the material is reduced from 1.85MPa to normal pressure after passing through the multi-section different-diameter material pipe to generate a vapor-liquid mixed polymer;
[0053] c. The vapor-liquid mixed polymer obtained in step b ...
Embodiment 3
[0066] A production method of high-elongation special-shaped nylon 66 fiber, comprising the following steps:
[0067] (1) Melt polymerization:
[0068] a. Transfer the nylon 66 salt solution to the concentration tank and heat it to 132°C for concentration, concentrate the nylon 66 salt solution with a mass percentage of 53% to a nylon 66 salt solution with a mass percentage of 72%, and discharge a large amount of water vapor;
[0069] b. The nylon 66 salt solution concentrated in step a is transported to the reactor (the reaction temperature is controlled at 255-268°C, the reaction time is controlled at 2.5~3.0h, and the reaction pressure is 1.85±0.5MPa) for high-pressure dehydration and polycondensation to form prepolymer then sent to the flash evaporator, the pressure of the material is reduced from 1.85MPa to normal pressure after passing through the multi-section different-diameter material pipe, and the vapor-liquid mixed polymer is generated;
[0070] c. The vapor-li...
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