Total reflux simulation of packed column distillation

被引:10
|
作者
Mori, H [1 ]
Ito, C [1 ]
Oda, A [1 ]
Aragaki, T [1 ]
机构
[1] Nagoya Inst Technol, Dept Appl Chem, Nagoya, Aichi 4668555, Japan
关键词
distillation; packed column; rate based model; total reflux; heat and mass transfer;
D O I
10.1252/jcej.32.69
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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 theta 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.
引用
收藏
页码:69 / 75
页数:7
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