Abstract
This study investigates the dynamics and control of discretely heat integrated distillation columns, focusing on two configurations: one utilizing a liquid pumparound loop and the other employing liquid injection for waste heat recovery in a multi-stage vapor recompression cycle. These innovative designs eliminate the need for vapor splitters, simplifying operation and enhancing control robustness. As case study, the methanol/water separation process was modelled to achieve 99.99 mol % purity for both products. Dynamic simulations were conducted in Aspen Dynamics to evaluate the control performance for ± 20 % throughput and composition disturbances. Results demonstrated that the proposed control structures, which rely on inferential temperature-based strategies, effectively maintain product specifications and ensure stable operation. This work provides valuable insights into the practical implementation of discretely heat integrated distillation columns, offering a pathway toward energy-efficient and operationally flexible distillation systems.
| Original language | English |
|---|---|
| Article number | 109144 |
| Pages (from-to) | 109144 |
| Journal | Computers and Chemical Engineering |
| Volume | 199 |
| DOIs | |
| Publication status | Published - Aug 2025 |
| MoE publication type | A1 Journal article-refereed |
Keywords
- Heat pump assisted distillation
- Process dynamics and control
- Process electrification
- Vapor recompression
- Waste heat recovery