| JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | |
| Total Reflux Simulation of Packed Column Distillation | |
| Tsutomu Aragaki1  Akiyoshi Oda1  Chikara Ito1  Hideki Mori1  | |
| [1] Department of Applied Chemistry, Nagoya Institute of Technology | |
| 关键词: Distillation; Packed Column; Rate Based Model; Total Reflux; Heat and Mass Transfer; | |
| DOI : 10.1252/jcej.32.69 | |
| 来源: Maruzen Company Ltd | |
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【 摘 要 】
References(11)Cited-By(7)This paper presents a simulation algorithm with a rate-based model for a packed distillation column at total reflux.The proposed algorithm consists of 1) composition and temperature profile calculation, which is slightly modified from the one for steady-state continuous distillation at finite reflux, and 2) composition correction for accelerating convergence with the overall θ method based on the component material balance considering liquid hold-up within the distillation column.Simulation results are compared with the experimental results of a ternary system obtained from a 0.21 m diameter packed distillation column. Fairly good agreement is obtained, though proper evaluation of the effective interfacial area and liquid hold-up distribution is essential for better simulation.
【 授权许可】
Unknown
【 预 览 】
| Files | Size | Format | View |
|---|---|---|---|
| RO201912080694504ZK.pdf | 19KB |
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