Preparation method of hindered phenol antioxidant
A technology of hindered phenols and antioxidants, applied in the field of preparation of polymer antioxidants, to achieve the effects of solving the three wastes problem, improving yield and product quality, and easy operation
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Embodiment 1
[0030]Put 450.0kg of triethylene glycol and 2150.0kg of 3-methyl-5-tert-butyl-4-hydroxyphenylpropionate methyl ester into a 3000L reaction kettle, heat up and stir, raise the temperature to 120°C, depressurize, and control the absolute pressure in the kettle To 10mmHg, heat preservation and stirring for 1h to remove light components in the material, and then release the pressure with nitrogen, add 2.25kg of lithium acetate catalyst under the protection of nitrogen, then close the nitrogen, carry out decompression reaction to extract methanol, and gradually increase the reaction temperature to 190°C, reduce the pressure in the reactor to 10mmHg, and then keep it under this pressure for 10h. After the reaction, the 245 content (HPLC) of the reaction solution is 91.5%, and the 345 ester content (HPLC) is 4.8%. Cool to 140°C, nitrogen After the pressure is released, put the material into the scraper evaporator for flash evaporation to evaporate the unreacted 345 ester. The temperat...
Embodiment 2
[0032] Put 450.0kg of triethylene glycol and 2050.0kg of 3-methyl-5-tert-butyl-4-hydroxyphenylpropionate methyl ester into a 3000L reaction kettle, heat up and stir, raise the temperature to 120°C, depressurize, and control the absolute pressure in the kettle To 10mmHg, heat preservation and stirring for 1h to remove the light components in the material, and then release the pressure with nitrogen, add 4.50kg of aluminum isopropoxide catalyst under the protection of nitrogen, then close the nitrogen, carry out decompression reaction to extract methanol, and gradually increase the reaction time by 1~2h Temperature to 160°C, reduce the pressure in the reactor to 1mmHg, and then keep the temperature under this pressure for 6h. After the reaction, the 245 content (HPLC) of the reaction solution is 92.9%, the 345 ester content (HPLC) is 3.2%, and the temperature is lowered to 100°C , after the nitrogen pressure is released, put the material into the scraper evaporator for flash evap...
Embodiment 3
[0034] Put 450.0kg of triethylene glycol and 2050.0kg of 3-methyl-5-tert-butyl-4-hydroxyphenylpropionate methyl ester into a 3000L reaction kettle, heat up and stir, raise the temperature to 120°C, depressurize, and control the absolute pressure in the kettle To 10mmHg, heat preservation and stirring for 1h to remove light components in the material, and then release the pressure with nitrogen, add 2.25kg of lithium acetate catalyst under the protection of nitrogen, then close the nitrogen, carry out decompression reaction to extract methanol, and gradually increase the reaction temperature to 160°C, reduce the pressure in the reactor to 5mmHg, and then keep it under this pressure for 8 hours. After the reaction, the 245 content (HPLC) of the reaction solution is 92.9%, and the 345 ester content (HPLC) is 3.2%. Cool to 100°C, nitrogen After the pressure is released, put the material into the scraper evaporator for flash evaporation to evaporate the unreacted 345 ester. The temp...
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