Preparation method of cycleanine
A technology of cyclamenine and products, which is applied in the field of preparation of cyclamenine, can solve the problems of cheap raw materials, long reaction time, few steps and the like, and achieves the effects of less solvent usage, simple operation and easy control.
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Embodiment 1
[0032] One-pot reaction:
[0033] 1m 3 After replacing the reactor with nitrogen, add 55kg of triethylenetetramine, 250kg of toluene, raise the temperature to 75°C, start adding 100kg of N,N'-dimethylformamide dimethyl acetal dropwise, and control the temperature in the kettle to 78°C-80°C ,Timing begins. After 0.5h, the system started to vacuum, and the vacuum degree gradually increased to 0.005MPa. After continuous extraction for 0.5h, the system vacuum degree was gradually increased to 0.05MPa, and the light components were completely recovered (produced fluid A), and the produced fluid A collected and recycled. Continue to discharge the liquid in the still, and the solid (intermediate product bis-imidazoline) stays in the still, and the discharged liquid is mixed with the production liquid A as the mother liquor to replace part of the toluene in the next batching in this step.
[0034] Then, add 650kg acetonitrile, 65kg dibromoethane, 30kg acid-binding catalyst in still...
Embodiment 2
[0039] Three kettles connected in series:
[0040] 2m 3After the reactor was replaced with nitrogen, 110kg of triethylenetetramine and 600kg of toluene were added, and the temperature was raised to 60°C. Start to drop 200kg of N,N'-dimethylformamide dimethyl acetal, control the temperature in the kettle to 70-75°C, and start timing. After 1 hour, the system was evacuated, and the vacuum gradually increased to 0.005MPa, and the extraction continued. After 1 hour, gradually increase the vacuum degree of the system to 0.05MPa, and completely extract the light components (production fluid A), and the production fluid A is collected and recycled. Continue to discharge and filter the suspension (intermediate product bis-imidazoline) in the kettle, and mix and collect the filtrate and the production liquid A to replace part of the toluene in the next batching in this step.
[0041] The obtained white solid was evaporated to dryness of toluene, and then sent to 10m 3 Reactor, add ...
Embodiment 3
[0046] Combined use of multiple kettles:
[0047] 1m 3 After the reactor was replaced with nitrogen, 55kg of triethylenetetramine and 600kg of toluene were added, and the temperature was raised to 55°C. Start to drop 110kg of N,N'-dimethylformamide dimethyl acetal, and control the temperature in the kettle to 55-65°C. After timing for 2 hours, the system is evacuated, and the vacuum gradually rises to 0.005MPa, and the extraction continues. After 0.5h, gradually increase the vacuum degree of the system to 0.05MPa, and completely extract the light components (production fluid A), and the production fluid A is collected and recycled. Continue to discharge and filter the suspension in the kettle, and the filtrate is mixed with the production liquid A to collect, and replace part of the toluene in the next batching in this step.
[0048] The obtained white solid was evaporated to dry toluene, and sent to two 1m 3 Reactor, add 700kg acetonitrile, 34kg dibromoethane, 16kg acid-b...
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