Method for continuous extraction distillation separation of dimethyl carbonate-methanol azeotropic mixture
A technology of dimethyl carbonate and azeotrope, which is applied in the field of continuous extraction, rectification and separation of dimethyl carbonate-methanol azeotrope, can solve the problems of high operating pressure, high energy consumption, increased investment cost of membrane separation devices, and the like, Achieve high yield and good separation effect
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Embodiment 1
[0011] Embodiment 1: adopt continuous rectification device, drop into the heating tank of extractive distillation tower azeotropic mixture dimethyl carbonate-methanol 500L (wherein methanol is 80%, dimethyl carbonate is 20%, all are mass percentages) , the selected extractant for the test is N,N-dimethylamide, open the heat source of the extractive distillation tower and the condensed water of the condenser, after the temperature of the top of the extractive distillation tower is stable, reflux for a period of time, and Add the extractant N, N-dimethylamide to the upper part of the tower, the ratio of extractant to feed is 2:5, when the temperature of the extractive distillation tower is 60-80°C, it will be distilled in the top of the extractive distillation tower Out methanol product, the reflux ratio is 3:1. When the bottom temperature of the extractive distillation tower is 80-120°C, the dimethyl carbonate-extractant distilled from the bottom of the tower is introduced into...
Embodiment 2
[0012] Embodiment 2: Experimental apparatus and operation method are with embodiment 1, and extractant adopts N-formylmorpholine.
Embodiment 3
[0013] Embodiment 3: The experimental device and operation method are the same as in Embodiment 1, and the extractant is an equal-volume mixture of N,N-dimethylamide and N-formylmorpholine.
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