A kind of polyester with low oligomer content and preparation method thereof
A technology of oligomer content, applied in the field of polymer materials, can solve the problems of reducing oligomer content in polyester, dyeing uniformity interference, etc., to achieve low oligomer content, low oligomer content, good The effect of applying the foreground
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Embodiment 1
[0048] A method for preparing polyester with low oligomer content, the steps are as follows:
[0049] (1) Add dimethyl terephthalate (291g), 1,4-butanediol (189g) and tetrabutyl titanate (0.7g) into a 2L polymerization reactor, and use vacuum / nitrogen circulation 3 times to complete It is possible to eliminate the residual air in the reactor and apply a slow nitrogen flow to the reaction system, then heat to 125°C to distill out the by-product methanol, and gradually increase the temperature to 190°C to maintain the esterification reaction until the amount of methanol evaporated reaches 95% of the theoretical value;
[0050] (2) Apply a vacuum to the reaction system to implement the first stage polycondensation reaction, the vacuum degree is 1KPa, the reaction temperature is set to 220°C, and the reaction time is 0.5h;
[0051] (3) Apply high vacuum to the reaction system (vacuum is 90Pa), and increase the reaction temperature to 260°C for the second-stage polycondensation reaction, ...
Embodiment 2
[0062] A method for preparing polyester with low oligomer content. The preparation steps are basically the same as in Example 1, except that the chain extender hexamethylene diisocyanate (15g) is added in step (5) for chain extension reaction .
[0063] The intrinsic viscosity and oligomer content of the final polyester are shown in Table 1.
Embodiment 3
[0065] A method for preparing polyester with low oligomer content, the steps are as follows:
[0066] (1) Add dimethyl terephthalate (310.7g), 1,4-butanediol (259.5g), tetrabutyl titanate (3.3g) and antioxidant 1010 (6.0g) into a 2L polymerization reactor ), use the vacuum / nitrogen cycle 3 times to remove the residual air in the reactor as much as possible, apply a slow nitrogen flow to the reaction system, then heat to 125°C to distill out the by-product methanol, and gradually increase the temperature to 190°C to maintain the esterification reaction until methanol The steam output reaches 95% of the theoretical value;
[0067] (2) Apply a vacuum to the reaction system to implement the first stage polycondensation reaction, the vacuum degree is 1KPa, the reaction temperature is set to 220°C, and the reaction time is 0.5h;
[0068] (3) Apply high vacuum to the reaction system (vacuum is 90Pa), and increase the reaction temperature to 260°C for the second-stage polycondensation react...
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