Copolyester and preparation method thereof
A technology of copolyester and esterification, which is applied in the field of copolyester, can solve problems such as poor adhesion, less polar functional groups, and large pollution, and achieve the effects of convenient processing, strong adhesion, and high strength
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Embodiment 1
[0038] A kind of preparation method of copolyester, first with dibasic monomer A (mass ratio is the mixture of terephthalic acid and isophthalic acid of 2:1) and dibasic monomer B (ethylene glycol) as raw material in Under the action of catalyst (antimony trioxide), carry out esterification reaction to obtain esterification product, then add multi-unit monomer C (trimellitic anhydride) and multi-unit monomer D (trimethylolpropane) in the catalyst (trimethylol propane) to the esterification product Under the effect of diantimony), polycondensation reaction is carried out, and copolyester is obtained; Wherein, the mol ratio of binary monomer A, binary monomer B, multi-element monomer C and multi-element monomer D is 1:1:0.28:0.3, In the esterification reaction, the amount of catalyst used is 30ppm of the sum of the quality of binary monomer A and binary monomer B, and the amount of catalyst used for polycondensation that continues to be added after the end of the esterification r...
Embodiment 2
[0042] A kind of preparation method of copolyester, earlier with dibasic monomer A (mass ratio is the terephthalic acid and isophthalic acid of 1:1) and dibasic monomer B (1,4-butanediol) as The raw material undergoes esterification reaction under the action of catalyst (antimony acetate) to obtain an esterified product, and then add multiple monomer C (pyromellitic dianhydride) and multiple monomer D (trimethylolpropane) to the esterified product Polycondensation reaction is carried out under the action of catalyst (antimony acetate) to obtain copolyester; wherein, the molar ratio of binary monomer A, binary monomer B, multi-component monomer C and multi-component monomer D is 1:1:0.26 : 0.28, catalyst consumption is 50ppm of the sum of binary monomer A and binary monomer B quality in the esterification reaction, and the catalyst amount that continues to add for polycondensation reaction after esterification finishes is 120ppm of multi-component monomer C quality ;
[0043] ...
Embodiment 3
[0046] A kind of preparation method of copolyester, first take binary monomer A (adipic acid) and binary monomer B (diethylene glycol) as raw material to carry out esterification reaction under the effect of catalyst (ethylene glycol antimony) to obtain Esterification product, then add multi-unit monomer C (trimellitic anhydride) and multi-unit monomer D (trimethylolpropane) to the esterification product to carry out polycondensation reaction under the action of catalyst (ethylene glycol antimony) to obtain copolyester; Wherein, the molar ratio of binary monomer A, binary monomer B, multi-component monomer C and multi-component monomer D is 1:1.2:0.24:0.26, and the amount of catalyst used in the esterification reaction is binary monomer A and binary monomer 70ppm of the sum of the monomer B quality, the amount of catalyst for polycondensation reaction that continues to be added after the end of the esterification reaction is 150ppm of the multi-component monomer C quality;
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