| 摘要 |
Polyalkylene terephthalates may be produced by the esterification of terephthalic acid with a glycol of the formula HO(CH2)nOH, where n is 2-10, in the presence of titanium dioxide in 0.01 to 0.2 per cent by weight of the terephthalic acid, as a catalyst and then further heating the monomeric terephthalate so formed, preferably with the application of a vacuum, without the addition of another catalyst. An example describes the preparation of a high molecular weight polyester using 0.025 parts of titanium dioxide per 50 parts of terephthalic acid, and heating with 300 parts of ethylene glycol to 195-196 DEG C., removing the water and excess ethylene glycol and then further heating to 275 DEG C. for one hour at a pressure of 15 mm. and a further 2 1/2 hours at a pressure of 1 mm. Other glycols which may be used are trimethylene glycol, butanediol-1,4, and decanediol-1,10.ALSO:Terephthalic acid is esterified with a glycol of the formula HO(CH2)nOH, where n is 2-10, in the presence of titanium dioxide as a catalyst in 0.01 per cent to 0.2 per cent by weight of the terephthalic acid. The reaction may be carried out batchwise or continuously. Terephthalic acid is preferably heated with an excess of glycol in the presence of titanium dioxide at a temperature of about 110 DEG -260 DEG C. after which the excess glycol is removed by distillation. The titanium dioxide may be employed in a finely divided or powdered form and dispersed directly into the reaction mixture, or may be dispersed in the glycol which may then be admixed with the terephthalic acid. The titanium dioxide can also act as an ester interchange catalyst thus the esterification and polymerization to high molecular weight polyesters may be carried out concurrently. Examples are given of the esterification of terephthalic acid and ethylene glycol. Other useful glycols are trimethylene glycol, butanediol 1,4 and decanediol-1,10. |
