A kind of preparation method of polyterephthalic acid isophthalic acid adipate/butylene glycol copolyester
A technology of polyterephthalic acid isophthalic acid and butanediol copolyester, which is applied in the field of preparation of biodegradable polymers, can solve the problems of low light transmittance, inability to meet the needs of use, poor whiteness, etc., and achieve High whiteness, excellent mechanical properties, and high intrinsic viscosity
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Embodiment 1
[0027] Add 24.8kg of terephthalic acid, 2.48kg of isophthalic acid, 19.4kg of adipic acid and 40kg of 1,4-butanediol into the reaction kettle, and perform esterification reaction at 160-240°C under an inert gas atmosphere. , when the temperature rises to 230°C, add 30g of tetrabutyl titanate (equivalent to 0.5‰ in the total weight of the product) to remove by-product water and generate adipate / butylene terephthalate isophthalate , when the total esterification rate reaches more than 95%, the esterification reaction ends; continue to add the compound of 24g phosphorous acid and triphenyl phosphate, and the weight ratio of the two is 2:1, (equivalent to the total weight of the product 0.4‰); then depressurize the reactor continuously to a high vacuum of 10-200Pa within 100 minutes. During this process, the by-product 1,4-butanediol is continuously distilled out. The vacuum polycondensation time is 1.5h, and then the reactor is returned to normal pressure with an inert gas to obt...
Embodiment 2
[0029] Add 24.8kg of terephthalic acid, 1.24kg of isophthalic acid, 19.4kg of adipic acid and 40kg of 1,4-butanediol into the reaction kettle, and perform esterification reaction at a temperature of 160-240°C under an inert gas atmosphere. , when the temperature rises to 230°C, add 30g of tetrapropyl titanate (equivalent to 0.05% of the total weight of the product) to remove by-product water and generate adipate / butylene terephthalate isophthalate , when the total esterification rate reaches more than 95%, the esterification reaction ends; continue to add 30g of tetrapropyl titanate (equivalent to 0.05% in the total product weight) and 30g of phosphorous acid and trimethyl phosphate compound, The weight ratio between the two is 1:2, (equivalent to 0.05% of the total weight of the product); then the reactor is continuously decompressed to a high vacuum of 10-200Pa within 100 minutes, and the by-product 1 is continuously distilled during this process. , 4-butanediol, the final r...
Embodiment 3
[0031] Add 24.8kg of terephthalic acid, 0.496kg of isophthalic acid, 19.4kg of adipic acid and 40kg of 1,4-butanediol into the reaction kettle, and perform esterification reaction at a temperature of 160-240°C under an inert gas atmosphere. , when the temperature rises to 230°C, add 54g of tetraisopropyl titanate (equivalent to 0.9‰ in the total weight of the product) to remove by-product water and generate terephthalic acid isophthalic acid adipate / butanediol ester, when the total esterification rate reaches more than 95%, the esterification reaction ends; continue to add the compound of 48g phosphoric acid and diethyl phosphite, and the weight ratio of the two is 1:1, (equivalent to the total product 0.8‰ of the weight); then the reactor was continuously decompressed to a high vacuum of 10-200Pa within 100 minutes. During this process, the by-product 1,4-butanediol was continuously distilled out. The high vacuum polycondensation time is 2 hours, and then the reactor is retur...
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