Method for separating allyl alcohol and water by extractive distillation with N-methyl-pyrrolidone
A methylpyrrolidone and extractive distillation technology, which is applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve the problems of high consumption of entrainer, long process flow, large process energy consumption, etc. Good economic and social benefits, simple separation process, low energy consumption
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Embodiment 1
[0026] Allyl alcohol and water raw material liquid 2 enter the middle part of the extractive distillation column 3 with a flow rate of 1000kg / hr, and the extractant N-methylpyrrolidone 1 enters the upper part of the extractive distillation column 3 according to the volume ratio of 2.5:1, and the theoretical plate number of this column is 40 blocks, the pressure at the top of the tower is 100kPa, the temperature at the top of the tower is 100°C, and the temperature at the bottom of the tower is 160°C. After the steam at the top of the tower is condensed by the condenser 5, water 5 with a product purity of 99.4wt% is extracted with a reflux ratio of 1:1. , the extractant solution 7 rich in allyl alcohol at the bottom of the tower enters the middle part of the solvent recovery tower 8, the number of theoretical plates of this tower is 50, the pressure at the top of the tower is 10kPa, the temperature at the top of the tower is 50°C, and the temperature at the bottom of the tower is...
Embodiment 2
[0028] Allyl alcohol and water raw material liquid 2 enter the middle part of the extractive distillation column 3 with a flow rate of 1000kg / hr, and the extractant N-methylpyrrolidone 1 enters the upper part of the extractive distillation column 3 according to a volume ratio of 3:1, and the theoretical plate number of this column is 42 blocks, the pressure at the top of the tower is 103kPa, the temperature at the top of the tower is 102°C, and the temperature at the bottom of the tower is 162.6°C. After the steam at the top of the tower is condensed by the condenser 5, water 5 with a product purity of 99.4wt% is extracted with a reflux ratio of 3:1. , the extraction agent solution 7 rich in allyl alcohol at the bottom of the tower enters the middle part of the solvent recovery tower 8, the number of theoretical plates of this tower is 55, the pressure at the top of the tower is 15kPa, the temperature at the top of the tower is 52°C, and the temperature at the bottom of the towe...
Embodiment 3
[0030] Allyl alcohol and water raw material liquid 2 enter the middle part of the extractive distillation column 3 with a flow rate of 1000kg / hr, and the extractant N-methylpyrrolidone 1 enters the upper part of the extractive distillation column 3 according to a volume ratio of 4:1, and the theoretical plate number of this column is 45 blocks, the pressure at the top of the tower is 105kPa, the temperature at the top of the tower is 105°C, and the temperature at the bottom of the tower is 165°C. After the steam at the top of the tower is condensed by the condenser 5, water 5 with a product purity of 99.4wt% is extracted with a reflux ratio of 5:1. , the extraction agent solution 7 rich in allyl alcohol at the bottom of the tower enters the middle part of the solvent recovery tower 8, the number of theoretical plates of this tower is 60, the pressure at the top of the tower is 20kPa, the temperature at the top of the tower is 55°C, and the temperature at the bottom of the tower ...
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