Ester exchange catalyst with biological activity, synthesis method of ester exchange catalyst, and application of ester exchange catalyst to preparation of degradable polyester
A transesterification catalyst and biologically active technology, applied in the field of transesterification catalysts, can solve the problems of not being able to apply synthetic biological polyester materials, increase the production cost of polyester materials, and cumbersome catalyst synthesis, and achieve good market space and value, excellent Catalytic activity, low cost effect
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Embodiment 1
[0050] (1) Add 10 grams of analytically pure 1,4-butanediol to a 250 mL three-necked flask equipped with a mechanical stirrer, a thermometer, a nitrogen gas inlet tube, a condenser, etc., add 0.35 grams of magnesium powder, and pass in argon, Heated to 120° C., reacted for 6 hours under stirring at 100 r.p.m, cooled and aged for 1 hour with stirring, to obtain 2.5 grams of magnesium butanediol with catalytic activity.
[0051] (2) Take another 250mL three-necked flask equipped with a mechanical stirrer, thermometer, nitrogen inlet tube, condenser, etc., add 16.3 grams of dimethyl succinate (112 mmol), 15 grams of 1,4-butanediol (166 mmol), fed with argon, gradually heated to 180°C, and reacted under stirring at 100r.p.m. The methanol produced was removed by condensation, and the reaction stopped when no methanol was produced.
[0052] (3) Cool down afterwards, add 0.35 gram of butanediol magnesium as transesterification catalyst. Then gradually raise the temperature to 230°C,...
Embodiment 2~5
[0066] The synthesis process is the same as in Example 1, except that the dimethyl succinate in the synthetic polyester process is replaced by dimethyl glutarate, dimethyl adipate, dimethyl pimelate, and suberic acid respectively. Dimethyl ester. The viscosity-average molecular weights of the obtained polyester products were 47kDa, 40kDa, 29kDa, and 22kDa, respectively.
Embodiment 6~9
[0068] Synthetic technique is the same as embodiment 1, and difference only is that the butanediol in synthetic polyester process is replaced with pentanediol, hexanediol, heptanediol, octanediol respectively. Transesterification catalyst is changed into corresponding glycol magnesium, and the viscosity-average molecular weight of gained polyester product is respectively 35kDa, 32kDa, 30kDa, 23 kDa.
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