Abstract
A model for an internally heat-integrated batch distillation column (Batch or Semi-batch HIDiC) was developed, and the separation of a benzene-toluene binary mixture was simulated. The applicability of the model was examined by using the commercial process simulator Aspen Plus Dynamics® to evaluate energy-saving performance and process time against the compression ratio and reflux ratio. The batch or semi-batch HIDiC model results were compared with the conventional batch distillation model. It was found that with the semi-batch HIDiC, the model has the potential to reduce process time and energy consumption more precisely than the conventional batch distillation model.
Original language | English |
---|---|
Pages (from-to) | 277-282 |
Number of pages | 6 |
Journal | Chemical Engineering Transactions |
Volume | 29 |
DOIs | |
Publication status | Published - 2012 |
Externally published | Yes |
ASJC Scopus subject areas
- Chemical Engineering(all)