Method for continuously synthesizing 5 (2-ethylthio propyl)-2-propionyl-3-hydroxyl-2-cyclohexene-1 ketone by using micro-channel reactor
A technology of microchannel reactor and ethylthiopropyl, which is applied in chemical instruments and methods, chemical/physical/physicochemical reactors, thioether preparation, etc., can solve the problem of high production cost, prone to side reactions, Low product content and other issues, to achieve the effects of no amplification effect, shortened production cycle, and high product yield
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Embodiment 1
[0035] The continuous synthesis method of 5(2 ethylthiopropyl)-2 propionyl-3 hydroxy-2 cyclohexene-1 ketone in the microchannel reactor of this embodiment includes:
[0036] The microchannel reactor is a three-stage reactor, and the microchannel reactor includes the first microchannel reactor, the second microchannel reactor and the third microchannel reactor communicated in sequence, and the third microchannel reactor The outlet port of the microchannel reactor is connected with the pipe reactor; the specific synthesis using this microchannel reactor includes the following contents:
[0037] The toluene solution (mass concentration is 24%) of acylate (compound 1) and the toluene solution (mass concentration is 5.5%) of DMAP are passed in the first stage microchannel reactor, and the flow velocity of the toluene solution of compound 1 is 3mL / min, the toluene solution flow rate of DMAP is 0.4mL / min, stay 7min at 150 ℃, the reaction solution enters the second-stage microchannel...
Embodiment 2
[0039] The continuous synthesis method of 5(2 ethylthiopropyl)-2 propionyl-3 hydroxy-2 cyclohexene-1 ketone in the microchannel reactor of this embodiment includes:
[0040] The microchannel reactor is a three-stage reactor, and the microchannel reactor includes the first microchannel reactor, the second microchannel reactor and the third microchannel reactor communicated in sequence, and the third microchannel reactor The outlet port of the microchannel reactor is connected with the pipe reactor; the specific synthesis using this microchannel reactor includes the following contents:
[0041]The toluene solution (mass concentration is 24%) of acylate (compound 1) and the toluene solution (mass concentration is 5.5%) of DMAP are passed in the first stage microchannel reactor, and the flow velocity of the toluene solution of compound 1 is 6mL / min, the toluene solution flow rate of DMAP is 0.8mL / min, stay at 160 ℃ for 3.5min, the reaction solution enters the second-stage microch...
Embodiment 3
[0043] The continuous synthesis method of 5(2 ethylthiopropyl)-2 propionyl-3 hydroxy-2 cyclohexene-1 ketone in the microchannel reactor of this embodiment includes:
[0044] The microchannel reactor is a three-stage reactor, and the microchannel reactor includes the first microchannel reactor, the second microchannel reactor and the third microchannel reactor communicated in sequence, and the third microchannel reactor The outlet port of the microchannel reactor is connected with the pipe reactor; the specific synthesis using this microchannel reactor includes the following contents:
[0045] The toluene solution (mass concentration is 24%) of acylate (compound 1) and the toluene solution (mass concentration is 5.5%) of DMAP are passed in the first stage microchannel reactor, and the flow velocity of the toluene solution of compound 1 is 6mL / Min, the toluene solution flow rate of DMAP is 0.8mL / min, stay 3.5min at 160 ℃, the reaction solution enters the second-stage microchann...
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