Continuous synthesis method of polyether
A synthetic method and technology of polyether, which is applied in the field of continuous synthesis of polyether prepared with small molecular alcohol as the initiator, and can solve the problems of wide molecular weight distribution of polyether
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Embodiment 1
[0026] Add 600g of 204 polyether and 0.09g of DMC catalyst into a 5L reaction kettle with an external circulation feeding pipe, replace with nitrogen three times, evacuate and heat up to 130°C, then pressurize to 0.000MPa and feed in 120g of propylene oxide until the pressure is obvious When the temperature drops and the temperature rises rapidly, it indicates that the DMC catalyst has been induced, and when the pressure drops below 0.003MPa, it indicates that the induction is over. Keep the temperature of the reactor at 140° C., and then continuously feed 2280 g of propylene oxide. Then continuously add the mixture of propylene glycol and propylene oxide (propylene glycol / propylene oxide weight ratio=72: 1928) in the reactor with the speed of 5000g / h, simultaneously DMC catalyst and 220 polyether carrier (in terms of carrier DMC concentration is 1500ppm ) is added continuously through the external circulation pipeline at a speed of 100g / h. Keep the pressure of the reactor at...
Embodiment 2
[0028] Add 400g of butyl polyether (molecular weight: 400) and 0.06g of DMC catalyst to a 5L reaction kettle with an external circulation feeding pipe, replace with nitrogen three times, vacuumize and raise the temperature to 110°C, then pressurize to 0.000MPa and pass through 80g of ring Propylene oxide, when the pressure drops significantly and the temperature rises rapidly, it indicates that the DMC catalyst has been induced, and when the pressure drops below 0.003MPa, it indicates that the induction is over. Keep the temperature of the reactor at 110° C., and then continuously feed 1520 g of propylene oxide. Then add the mixture of n-butanol and propylene oxide (n-butanol / propylene oxide=74: 1926) continuously in the reactor with the speed of 10000g / h, simultaneously DMC catalyst and butyl polyether (molecular weight 2000) carrier ( DMC concentration (15000ppm in terms of carrier) is continuously added through the external circulation pipeline at a speed of 20g / h. Keep th...
Embodiment 3
[0030] Add 600g of butyl polyether (molecular weight: 2000) and 0.09g of DMC catalyst to a 5L reaction kettle with an external circulation feeding pipe, replace with nitrogen three times, vacuumize and raise the temperature to 120°C, then pressurize to 0.000MPa and pass through a 120g ring Propylene oxide, when the pressure drops significantly and the temperature rises rapidly, it indicates that the DMC catalyst has been induced, and when the pressure drops below 0.003MPa, it indicates that the induction is over. Keep the temperature of the reactor at 120° C., and then continuously feed 2280 g of propylene oxide. Then add the mixture of n-butanol and propylene oxide (n-butanol / propylene oxide=74:9928.4) continuously in the reactor with the speed of 4000g / h, simultaneously DMC catalyst and butyl polyether (molecular weight 2000) carrier ( DMC concentration (3000ppm in terms of carrier) is continuously added through the external circulation pipeline at a speed of 40g / h. Keep th...
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