Breaking Azeotropes with Hybrid Separation Systems
Breaking Azeotropes with Hybrid Separation Systems
Consider a binary mixture of isopropanol and water at This mixture exhibits a positive azeotrope at isopropanol, which limits the separation that can be achieved using a single distillation column. One way to break the azeotrope is to add a membrane separator, shown by selecting "hybrid setup".
101.325kPa.
69.8mole%
This Demonstration shows that you can obtain a product stream and a saturated liquid reflux stream with isopropanol. The column now can achieve a top vapor stream with a composition of isopropanol (because of the isopropanol-rich reflux stream). The recycle stream and the feed stream have compositions equal to and isopropanol, respectively. Feed, a saturated vapor, has a flow rate equal to . CMO (constant molal overflow) is assumed. You can set the value of the internal reflux ratio to display the corresponding McCabe and Thiele construction.
96mole%
80 mole %
40
20mole%
1000kg-mole/hr