Method for preparing N,N-dimethyl-(R)-1-[(S)-2-(diphenylphosphine)ferrocenyl]ethylamine by microreactor
A technology of ferrocene and diphenylphosphine, which is applied in the field of N preparation, can solve the problems of complex reaction operation process and by-product generation, and achieve the effects of improving reaction efficiency, improving yield and reducing cost.
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Embodiment 1
[0026] (1) Raw material storage tanks 1 and 4 are respectively the methyl tert-butyl ether solution of N,N-dimethyl-(R)-1-[(S)-ferrocenyl]ethylamine (mass fraction 15% ) and n-butyllithium in n-hexane (2.7M), the methyl tert-butyl group of N,N-dimethyl-(R)-1-[(S)-ferrocenyl]ethylamine is controlled by a metering pump The flow rate of the ether solution is 50mL / min, and the flow rate of n-butyllithium n-hexane solution is 12mL / min, which is injected into the constant temperature module of the microchannel reactor and treated at a constant temperature of 25°C; after the constant temperature treatment, it enters the first mixing module of the microchannel reactor for Reaction, reaction temperature 25°C, residence time 7.1s.
[0027] (2) The effluent of the first mixing module is reacted with diphenylphosphine chloride in the second mixing module, the flow rate of diphenylphosphine chloride is controlled by a metering pump to be 7mL / min, the reaction temperature is 35°C, and the ...
Embodiment 2
[0030] (1) Raw material storage tanks 1 and 4 are respectively the methyl tert-butyl ether solution of N,N-dimethyl-(R)-1-[(S)-ferrocenyl]ethylamine (mass fraction 15% ) and n-butyllithium in n-hexane (2.7M), the methyl tert-butyl group of N,N-dimethyl-(R)-1-[(S)-ferrocenyl]ethylamine is controlled by a metering pump The flow rate of ether solution is 50mL / min, and the flow rate of n-butyllithium n-hexane solution is 14mL / min, which is injected into the constant temperature module of the microchannel reactor for constant temperature treatment at 25°C; after constant temperature treatment, it enters the first mixing module of the microchannel reactor for Reaction, reaction temperature 25°C, residence time 10.7s.
[0031] (2) The effluent of the first mixing module is reacted with diphenylphosphine chloride in the second mixing module, the flow rate of diphenylphosphine chloride is controlled by a metering pump to be 7mL / min, the reaction temperature is 35°C, and the Time 9.8s....
Embodiment 3
[0034] (1) Raw material tanks 1 and 4 are respectively the methyl tert-butyl ether solution of N,N-dimethyl-(R)-1-[(S)-ferrocenyl]ethylamine (mass fraction 20% ) and n-butyllithium in n-hexane (1.8M), the methyl tert-butyl group of N,N-dimethyl-(R)-1-[(S)-ferrocenyl]ethylamine is controlled by a metering pump The flow rate of the ether solution is 75mL / min, and the flow rate of n-butyllithium n-hexane solution is 39mL / min, which is injected into the constant temperature module of the microchannel reactor and treated at a constant temperature of 25°C; after the constant temperature treatment, it enters the first mixing module of the microchannel reactor for Reaction, reaction temperature 25°C, residence time 3.6s.
[0035] (2) React the effluent of the first mixing module with diphenylphosphine chloride in the second mixing module, the flow rate of diphenylphosphine chloride is controlled by a metering pump to be 12mL / min, the reaction temperature is 35°C, and the Time 3.4s. ...
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