Para-aramid precipitation fiber and continuous production method thereof
A production method, para-aramid technology, applied in the field of para-aramid precipitated fiber and its continuous production, can solve the problem of long process flow
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Embodiment 1
[0067] (1) Under the condition of nitrogen protection, through the transfer pump to 1m 3 Put dehydrated NMP750L into the dissolution kettle, then add 46.26kg of calcium chloride under stirring, dissolve at 93°C, and obtain a calcium chloride solution after dissolving for 35min, then lower the temperature in the dissolution kettle to 0°C; then Add 16.23kg p-phenylenediamine (PPD) under stirring, stir and dissolve for 45min to obtain p-phenylenediamine solution;
[0068] (2) The p-phenylenediamine solution and the terephthaloyl chloride melt kept at 105°C are precisely metered by a metering pump, and then directly transported to a twin-screw reactor by a delivery pump for polymerization, wherein the precise control is carried out by a metering pump The molar ratio of terephthaloyl chloride and p-phenylenediamine into the screw reactor is (1.00~1.005):1;
[0069] The length-to-diameter ratio of the twin-screw reactor is 40:1, the rotation speed is 200 rpm, and the outlet tempera...
Embodiment 2
[0075] (1) Under the condition of nitrogen protection, through the transfer pump to 1m 3 Put dehydrated NMP750L into the dissolution kettle, then add 30.84kg magnesium chloride under stirring, dissolve at 90°C, and obtain a magnesium chloride solution after dissolving for 40min, then lower the temperature in the dissolution kettle to 5°C; then add 32.45kg p-phenylenediamine (PPD), stirring and dissolving 40min, obtains p-phenylenediamine solution;
[0076] The p-phenylenediamine solution and the terephthaloyl chloride melt kept at 107°C are accurately metered by a metering pump, and then directly transported to the twin-screw reactor by a delivery pump for polymerization. The molar ratio of formyl chloride and p-phenylenediamine added to the screw reactor is (1.00~1.003):1;
[0077] The length-to-diameter ratio of the twin-screw reactor is 50:1, the rotation speed is 150 rpm, and the outlet temperature at the end of the screw is kept below 70°C. The twin-screw reactor has tw...
Embodiment 3
[0082] (1) Under the condition of nitrogen protection, through the transfer pump to 1m 3 Put 750L of dehydrated DMAc into the dissolution kettle, then add 61.68kg of aluminum chloride under stirring, dissolve at 94°C, and obtain a lithium chloride solution after dissolving for 35min, then lower the temperature in the dissolution kettle to -3°C; Then add 48.65kg p-phenylenediamine (PPD) under stirring, stir and dissolve for 50min to obtain p-phenylenediamine solution;
[0083] (2) The p-phenylenediamine solution and the terephthaloyl chloride melt kept at 103°C are accurately metered by a metering pump, and then directly transported to a twin-screw reactor by a delivery pump for polymerization. The molar ratio of terephthaloyl chloride and p-phenylenediamine into the screw reactor is (1.00~1.008):1;
[0084] The length-to-diameter ratio of the twin-screw reactor is 55:1, the rotation speed is 80 rpm, and the outlet temperature at the end of the screw is kept below 70°C. The t...
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