Abstract
Dehydration via batch heteroazeotropic distillation emerges as a promising technology for the recovery of acetic acid (HAc) from dilute aqueous solutions. In this preliminary work, this process was studied with the aid of Aspen Batch Modeler®, using an acetic acid aqueous solution as the model feed instead of wood vinegar from biorefineries and n-butyl acetate as the azeotropic entrainer. The non-random two liquids (NRTL)-virial Hayden-O'Connell model (HOC) model was chosen to calculate the thermodynamic properties. The response surface methodology with Box-Behnken design was successfully applied to obtain optimum process conditions, providing a dehydrated HAc product from the pot with high purity and recovery.
| Original language | English |
|---|---|
| Pages (from-to) | 477-487 |
| Number of pages | 11 |
| Journal | Chemical Engineering and Technology |
| Volume | 44 |
| Issue number | 3 |
| DOIs | |
| Publication status | Published - Mar 2021 |
| Externally published | Yes |
Free Keywords
- Batch heteroazeotropic distillation
- Box-Behnken design
- Dilute acetic acid
- Process simulations
- n-Butyl acetate
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering