Polyester resin and process for its production
a polymer resin and polymer technology, applied in the field of polymer resin, can solve the problems of reduced aroma-retention property, high cost of germanium compound, and low UV shielding property
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example 1
[0054] Slurries of 43 kg (260 mol) of terephthalic acid and 19 kg (312 mol) of ethylene glycol were continuously supplied over a period of 4 hours to an esterification reaction tank having about 60 kg of bis(hydroxyethyl) terephthalate previously charged and maintained at a temperature of 250° C. and a pressure of 1.2×105 Pa, and even after completion of the supply, the esterification reaction was further carried out for one hour. About one half of this esterification reaction product was transferred to a polycondensation tank.
[0055] Then, to the polycondensation tank to which the esterification reaction product was transferred, from its pipe, ethyl acid phosphate, magnesium acetate and tetra-n-butoxy titanium were sequentially added in their ethylene glycol solutions, respectively, with intervals of 5 minutes, so that 0.387 mol of phosphorus atoms (P), 0.062 mol of magnesium atoms (Mg) and 0.063 mol of titanium atoms (Ti) would remain per 1 ton of the resulting polyester resin. Th...
examples 2 to 6
[0077] The operation was carried out in the same manner as in Example 1 except that the amounts of ethyl acid phosphate, magnesium acetate and tetra-n-butoxy titanium at the time of the melt polycondensation were changed as shown in Table 1, and then results are shown in Table 1.
example 7
[0078] The operation was carried out in the same manner as in Example 2 except that the solid phase polycondensation polyester resin obtained in Example 2 was further subjected to water treatment by immersing it in hot water of 90° C. for two hours, and the results are shown in Table 1.
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