Abstract
Process data of a commercial-scale batch distillation column for separation of a ternary mixture of 2-propanol/ water/n-hexane was analyzed, and a simulation model capable of predicting dynamic conditions was developed. The developed model was applied to batch distillation in a commercial plant, and the operation performances were studied. By adjusting the conventional operating conditions, it was found possible to improve the function and performance of the process and achieve energy-saving.
| Original language | English |
|---|---|
| Pages (from-to) | 350-354 |
| Number of pages | 5 |
| Journal | kagaku kogaku ronbunshu |
| Volume | 44 |
| Issue number | 6 |
| DOIs | |
| Publication status | Published - 2018 |
| Externally published | Yes |
Keywords
- Azeotropic Distillation
- Batch Process
- Commercial Plant
- Reflux Ratio
- Simulation
ASJC Scopus subject areas
- Chemistry(all)
- Chemical Engineering(all)