抄録
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.
本文言語 | English |
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ページ(範囲) | 350-354 |
ページ数 | 5 |
ジャーナル | kagaku kogaku ronbunshu |
巻 | 44 |
号 | 6 |
DOI | |
出版ステータス | Published - 2018 |
外部発表 | はい |
ASJC Scopus subject areas
- 化学 (全般)
- 化学工学(全般)