Alkaline soluble polyester and preparation method thereof
A technology of alkali-soluble polyester and polyester, applied in the field of polyester with alkali water solubility and its preparation, can solve the problem of increasing the internal rotation activation energy of macromolecules, reducing the movement capacity of macromolecular chains, and increasing molecular chain entanglement points and other problems, to achieve the effect of excellent spinning operability, uniform and continuous spinning, and shortened polycondensation time
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Embodiment 1
[0024] First, 1000 parts by weight of purified terephthalic acid and 430 parts by weight of ethylene glycol are added to the beating kettle, and 0.58 parts by weight of anti-etherification agent sodium acetate is added, and continuously enter the esterification kettle, and carry out esterification under normal pressure at 240°C to 260°C; Until the water effluent terminates the esterification. Then to the polymerization tank, add 96.3 parts by weight of EG solution of ethylene glycol isophthalate-5-sodium sulfonate, add 46.4 parts by weight of 1,6-hexanediol after stirring for several minutes, and add 0.35 parts by weight of catalyst containing Sb compound parts, and 0.23 parts by weight of composite stabilizer IR1010, 0.35 parts by weight of cobalt acetate, and 0.29 parts by weight of phosphoric acid. Under the action of a vacuum pump, keep the vacuum degree below 200Pa to carry out the polymerization reaction, and the temperature is controlled at 270 ° C ~ 280 ° C. , Diced. ...
Embodiment 2
[0026] First, 1000 parts by weight of purified terephthalic acid and 430 parts by weight of ethylene glycol are added to the beating kettle, and 0.58 parts by weight of anti-etherification agent sodium acetate is added, and continuously enter the esterification kettle, and carry out esterification under normal pressure at 240°C to 260°C; Until the water effluent terminates the esterification. Then the polymerization tank, add 192.5 parts by weight of EG solution of ethylene glycol isophthalate-5-sodium sulfonate, add 46.2 parts by weight of adipic acid after stirring for several minutes, and add 0.35 parts by weight of catalyst containing Sb compound, and compound 0.23 parts by weight of stabilizer IR1010, 0.35 parts by weight of cobalt acetate, and 0.29 parts by weight of phosphoric acid. Under the action of a vacuum pump, keep the vacuum degree below 200 Pa to carry out the polymerization reaction, and the temperature is controlled at 270 ° C to 280 ° C.
Embodiment 3
[0028] First, 1000 parts by weight of purified terephthalic acid and 430 parts by weight of ethylene glycol are added to the beating kettle, and 0.58 parts by weight of anti-etherification agent sodium acetate is added, and continuously enter the esterification kettle, and carry out esterification under normal pressure at 240°C to 260°C; Until the water effluent terminates the esterification. Then, add 288.8 parts by weight of EG solution of ethylene glycol isophthalate-5-sodium sulfonate to the polymerization tank, add 23.1 parts by weight of adipic acid after stirring for several minutes, and add 1,6-hexanedioic acid after stirring for several minutes. 23.2 parts by weight of alcohol, and add 0.35 parts by weight of catalyst containing Sb compound, and 0.23 parts by weight of composite stabilizer IR10100, 0.35 parts by weight of cobalt acetate, 0.29 parts by weight of phosphoric acid, under the action of vacuum pump, keep the vacuum degree below 200Pa to carry out polymerizat...
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