Method for producing polyester and polyester mixture
A manufacturing method and a mixture technology, which are applied to polyesters with fast crystallization properties without adding a nucleating agent and their production fields, can solve the problems of accelerating the crystallization rate of PET, difficulty in recycling, slow crystallization rate of ethylene terephthalate, etc. problems, to achieve the effect of reducing the processing difficulty and time, and increasing the crystallization rate
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Embodiment 1
[0039] 1873.8 grams of ethylene terephthalate monomer and 936.9 grams of terephthalic acid were placed in the reactor, and the esterification reaction was carried out in a nitrogen atmosphere to form a first polyester mixture. The nitrogen atmosphere is pressurized with nitrogen to replace the air in the reactor. The esterification reaction is carried out under normal pressure at 260°C. Afterwards, 0.748 grams of antimony trioxide and 3.75 grams of ethylene glycol solution containing 5 wt % phosphoric acid were added to the first polyester mixture to carry out a superposition reaction to form a second polyester mixture. The coincidence reaction was carried out at 275°C until the intrinsic viscosity of the second polyester mixture was greater than 0.57.
Embodiment 2
[0041] Put 1080.8 grams of terephthalic acid, 403.7 grams of ethylene glycol, 1653.7 grams of ethylene terephthalate monomer and 1.25 grams of tetraethylammonium hydroxide into the reactor for esterification to form a first polyester mixture. The esterification reaction is at 260°C and 2kg / cm2 under nitrogen pressure. Afterwards, 0.748 grams of antimony trioxide and 3.75 grams of ethylene glycol solution containing 5 wt % phosphoric acid were added to the first polyester mixture to carry out a superposition reaction to form a second polyester mixture. The coincidence reaction was carried out at 275°C until the intrinsic viscosity of the second polyester mixture was greater than 0.57.
Embodiment 3
[0051] The second polyester mixture of Example 1 was blended with the second polyester mixture of Comparative Example 4 to obtain the second polyester mixture of Example 3.
[0052] The following table 1 is the data of Examples 1-3 and Comparative Examples 1-4 of the present invention, listing respectively the intrinsic viscosity of the second polyester mixture, the content of diethylene glycol in the second polyester mixture, the second polyester mixture The polydispersity index of the polyethylene terephthalate, the crystallization melting point, the crystallization temperature and the degree of supercooling of the polyethylene terephthalate of the second polyester mixture. To further illustrate, the degree of supercooling is the difference between the crystallization melting point minus the crystallization temperature, and the degree of supercooling is an index used to measure the crystallization difficulty of polymers. The smaller the degree of undercooling, the shorter th...
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