Melt direct spinning porous superfine polyester fiber and preparation method thereof
A technology of superfine polyester fiber and melt direct spinning, applied in the field of polyester spinning, can solve the problems affecting the quality of melt direct spinning porous superfine polyester fiber, short replacement cycle of filters and spinning components, etc. Achieve excellent breaking strength and elongation at break, improve filtration performance, and extend the effect of replacement cycle
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[0043] For this reason, the present invention provides a kind of preparation method of melt direct spinning porous superfine polyester fiber, specifically, in terephthalic acid and ethylene glycol esterification reaction, add sodium borohydride, after esterification reaction, then Melt direct spinning porous superfine polyester fiber is obtained through polycondensation reaction and spinning process.
[0044] Specifically, the preparation method includes:
[0045] S1. Make a slurry of terephthalic acid and ethylene glycol, add sodium borohydride, catalyst and stabilizer and mix evenly, and then carry out esterification reaction. The temperature of the esterification reaction is 200-260°C, and the time is 120-180min. , during the esterification reaction, the temperature gradually increased from 200°C to 260°C and finally kept at 260°C;
[0046] S2. After the esterification reaction is completed, the polycondensation reaction is carried out under negative pressure conditions be...
Embodiment 1
[0073] Step 1. Make a slurry of terephthalic acid and ethylene glycol, add sodium borohydride, catalyst and stabilizer and mix evenly, and then carry out esterification reaction. The temperature of the esterification reaction is 220-260° C., and the time is 120 minutes. During the esterification reaction, the esterification temperature is a process of gradually increasing the temperature, and the temperature gradually rises from 200°C to 260°C and is finally maintained at 260°C.
[0074] The molar ratio of terephthalic acid and ethylene glycol is 1:1.3;
[0075] The addition amount of catalyst antimony trioxide is 0.01% of the weight of terephthalic acid; the addition amount of sodium borohydride is 30 ppm of the weight of terephthalic acid; the addition amount of stabilizer triphenyl phosphate is 0.01% of the weight of terephthalic acid. %.
[0076] Step 2: After the esterification reaction is completed, the polycondensation reaction is carried out under a negative pressure ...
Embodiment 2
[0089] Step 1. Make a slurry of terephthalic acid and ethylene glycol, add sodium borohydride, catalyst and stabilizer and mix evenly, then carry out esterification reaction. The temperature of the esterification reaction is 220-260° C. and the time is 180 minutes. During the esterification reaction, the esterification temperature is a process of gradually increasing the temperature, and the temperature gradually rises from 200°C to 260°C and is finally maintained at 260°C.
[0090] The molar ratio of terephthalic acid and ethylene glycol is 1:1.5;
[0091] The addition of catalyst ethylene glycol antimony is 0.02% of the weight of terephthalic acid; the addition of sodium borohydride is 50ppm of the weight of terephthalic acid; the addition of stabilizer trimethyl phosphate is 0.03% of the weight of terephthalic acid %.
[0092] Step 2: After the esterification reaction is completed, the polycondensation reaction is carried out under negative pressure conditions with an abso...
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