Microfilm evaporator, rectifying system including same and rectifying method utilizing same
An evaporator and micro-film technology, applied in the field of rectification process and micro-film evaporator, can solve the problems of unsatisfactory heat exchange efficiency, slow component separation, incomplete component separation, etc., to save installation space , The effect of long residence time and easy and flexible installation
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Embodiment 1
[0052] The present invention is used for evaporative purification of vitamin E. First, the vitamin E product is extracted with petroleum ether, and then the petroleum ether containing vitamin E is passed into the middle of the rectification tower 3, and the outer sides of the rectification tower 3 are respectively connected to the top of the rectification tower to condense Device 8 reflux tank 7, tower top product storage tank 6, metering pump 4 for rectification tower kettle, microfilm evaporator 5; after the petroleum ether of vitamin E is through sufficient gas-liquid exchange in rectification tower 3, the boiling point is at 30 The components at -80°C enter the condenser 8 from the top of the tower and then enter the reflux tank 7 at the top of the rectification tower. Part of the material in the reflux tank 7 returns to the rectification tower 3 for reflux, and part of it is extracted as the top product, and the rectification tower 3 The components with a boiling point hig...
Embodiment 2
[0054] The present invention is used in the acetone recovery section of the acetylacetone preparation process, and the mixed gas of acetone and isopropenyl acetate after crude distillation is condensed and passed into the middle part of the rectification tower 3, and the outer sides of the rectification tower 3 are respectively connected to the rectification tower Top condenser 8, reflux tank 7, tower top product storage tank 6, metering pump 4 for rectification tower still, microfilm evaporator 5; After the gas-liquid exchange, the components with a boiling point of 50-58°C enter the condenser 8 from the top of the tower and then enter the reflux tank 7 at the top of the rectification tower. Part of the material in the reflux tank 7 returns to the rectification tower 3 for reflux, and part of it is recovered. As the tower top product, the components with a boiling point ≥ 60°C in the rectification tower 3 fall into the lower tower kettle, and are pumped into the microfilm evap...
Embodiment 3
[0056] The present invention is used for the continuous rectification and separation of propylene carbonate crude product, the operating temperature is 90°C, and the propylene carbonate crude product with a product purity of 98% enters the middle part of the rectification tower 3, and the outside of the rectification tower 3 is respectively connected to the rectification tower Top condenser 8, reflux tank 7, tower top product storage tank 6, metering pump for rectification tower kettle 4, microfilm evaporator 5; after the crude propylene carbonate undergoes sufficient gas-liquid exchange in rectification tower 3, its boiling point The fraction at 80-100°C enters the condenser 8 from the top of the tower, and then enters the reflux tank 7 at the top of the rectification tower. Part of the material in the reflux tank 7 returns to the rectification tower 3 for reflux, and a part is extracted as the top product for rectification. The components with a boiling point ≥ 110°C in the t...
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