A kind of barrier polyester and preparation method thereof
A barrier and polyester technology, applied in the field of barrier polyester and its preparation, can solve the problems of short processing flow, affecting the physical and chemical properties of PET, low energy consumption, etc., and achieve the goal of increasing the degree of crosslinking and reducing the oxygen transmission rate Effect
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[0016] The preparation method of the polyester provided by the invention comprises mixing terephthalic acid, ethylene glycol and a barrier comonomer, performing an esterification reaction in the presence of a catalyst, and then performing a polycondensation reaction after heating up.
[0017] In the above method, the molar ratio of carboxyl groups to hydroxyl groups in terephthalic acid, ethylene glycol and barrier comonomers, that is, the molar ratio of total carboxyl groups to total hydroxyl groups contained in the reactants is 1:1.0~1.8, preferably 1:1.1~ 1.5.
[0018] The mole percentage of the hydroxyl and carboxyl groups (the sum of the two) provided by the barrier comonomer to the total hydroxyl and carboxyl groups (the sum of the two) of the reactants is 0.5-10 mol%, preferably 0.5-5 mol%.
[0019] The preparation method of the barrier polyester provided by the present invention is divided into two steps. The first step is an esterification reaction between small molec...
example 1
[0025] Add 415.0g (2.50mol) of terephthalic acid, 184.1g (2.97mol) of ethylene glycol, 4.44g (0.03mol) of 3,5-dihydroxyhexanoic acid and 0.2g of catalyst antimony acetate into the autoclave. The gas in the kettle was replaced twice. The esterification reaction was carried out at 230° C. for 2 hours under a pressure of 0.1 MPa and stirring. The temperature was raised to 280°C, and the polycondensation reaction was carried out under reduced pressure for 2 hours. The polyester product was collected, and its properties are shown in Table 1. The polyester contained 0.8% by mass of 3,5-dihydroxyhexanoic acid.
example 2
[0027] Add 415.0g (2.50mol) of terephthalic acid, 180.4g (2.91mol) of ethylene glycol, 13.32g (0.09mol) of 3,5-dihydroxyhexanoic acid and 0.2g of catalyst antimony acetate into the autoclave. The gas in the kettle was replaced twice. The esterification reaction was carried out at 230° C. for 1 hour under a pressure of 0.1 MPa and stirring. The temperature was raised to 280°C, and a polycondensation reaction was performed under reduced pressure for 1 hour. The polyester product was collected, and its properties are shown in Table 1. The polyester contained 2.2% by mass of 3,5-dihydroxyhexanoic acid.
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