Method for synthesizing PBT polyester
A technology of polyester and mixture, applied in the field of polyester production, can solve the problems of uneven catalyst feed, precipitation, and poor solubility of titanium series
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Embodiment 1
[0023] Step 1: At room temperature and room pressure, place 13.45g (38.5mmol) of an aqueous solution with a citric acid content of 55% in a flask, slowly add 6.66g (19.6mmol) of TBT dropwise while stirring, and continue at room temperature after the addition is complete Stir at low temperature until the solution is uniform, then add 0.42 g (1.96 mmol) of solid magnesium acetate tetrahydrate, stir at room temperature to dissolve it, and form a turbid liquid without solid particles. Move the turbid liquid into a separatory funnel and let it stand for stratification, and separate the lower liquid to obtain catalyst 1. The titanium content of the obtained catalyst 1 is about 6.2%, and the pH of the catalyst 1 is ≈1;
[0024] Step 2: 35g terephthalic acid and 32.25g1,4-butanediol (ratio of the amount of substance is 1 to 1.7) are placed in the reactor with stirring, condensing and splitting and decompression device, catalyst 1 consumption is 280ppm (the amount of titanium relative ...
Embodiment 2
[0026] Step 1: At room temperature and pressure, put 25.41g (72.7mmol) of 55% citric acid aqueous solution in a flask, slowly add 9.91g (29.1mmol) of TBT dropwise while stirring, and continue at room temperature after the addition is complete Stir at low temperature until the solution is uniform, then add 6.24 g (29.1 mmol) of solid magnesium acetate tetrahydrate, stir at normal temperature to dissolve it, and form a turbid liquid without solid particles, which is moved into a separatory funnel and allowed to stand for layering. The catalyst 2 is obtained by separating the liquid in the lower layer. The titanium content of the obtained catalyst 2 is about 3.9%, and the pH of the catalyst liquid is ≈2.
[0027] Step 2: 35g terephthalic acid, 32.25g 1,4-butanediol (mol ratio is 1 to 1.7) is placed in the reactor that has stirring, condensing split flow and decompression device, and catalyst 2 consumption is 280ppm ( The amount of titanium relative to the amount of terephthalic a...
Embodiment 3
[0029] Step 1: At room temperature and room pressure, dissolve 3.55g of lactic acid (39.4mmol) and citric acid 7.51 (39.1mmol) in 10g of aqueous solution and place in a flask, slowly add TBT 6.66g (19.6g) dropwise while stirring, drop After the addition, continue to stir at room temperature until the solution is uniform, then add 1.64 g (39 mmol) of solid lithium hydroxide monohydrate, stir at room temperature to dissolve it, and form a turbid liquid without solid particles. Transfer the turbid liquid into a separatory funnel, let it stand for stratification, and separate the lower liquid to obtain catalyst 3. The titanium content of the obtained catalyst 3 is about 3.5%, and the pH of the catalyst liquid is ≈1.
[0030] Step 2: 35g terephthalic acid, 32.25g 1,4-butanediol (mol ratio is 1 to 1.7) is placed in the reactor that has stirring, condensing and splitting and pressure reducing device, and catalyst 3 consumption is 280ppm ( The amount of titanium relative to terephthal...
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