抄録
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.
本文言語 | English |
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ページ(範囲) | 277-282 |
ページ数 | 6 |
ジャーナル | Chemical Engineering Transactions |
巻 | 29 |
DOI | |
出版ステータス | Published - 2012 |
外部発表 | はい |
ASJC Scopus subject areas
- 化学工学(全般)