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 |
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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 |
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