Packed column distillation simulation with a rate-based method

被引：13
|
作者：
Mori, H
Oda, A
Aragaki, T
Kunimoto, Y
机构：
[1] Department of Applied Chemistry, Nagoya Institute of Technology
来源：
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | 1996年 / 29卷 / 02期
关键词：
distillation; packed column; rate based model; multicomponent; heat and mass transfer;
D O I：
10.1252/jcej.29.307
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
A simulation algorithm using a rate-based model is proposed for multicomponent packed column distillation. The packed column sections are divided into small segments for the modeling. For each packing segment, (6c + 7) MERQ equations are set up and solved by an equation-tearing method with two calculation loops. Calculation of the whole column consists of an iterative segment-wise algorithm with the correction of the bulk vapor composition by the overall normalized theta method for acceleration. The numerical characteristics of the proposed algorithm and some remarks on its application are illustrated using numerical examples and experimental data obtained from a pilot-scale plant.
引用
收藏
页码：307 / 314
页数：8
相关论文
共 50 条
  • [1] Packed column distillation simulation with a rate-based method (vol 29, pg 310, 1996)
    Mori, H
    [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1996, 29 (06) : 1080 - 1080
  • [2] Dynamic rate-based and equilibrium models for a packed reactive distillation column
    Peng, JJ
    Edgar, TF
    Eldridge, RB
    [J]. CHEMICAL ENGINEERING SCIENCE, 2003, 58 (12) : 2671 - 2680
  • [3] Rate-based modelling and simulation of pilot scale distillation column
    May-Vazquez, Mayra M.
    Gomez-Castro, Fernando I.
    Rodriguez-Angeles, Mario A.
    [J]. 29TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PT A, 2019, 46 : 625 - 630
  • [4] Sequential simulation of packed distillation columns using rate-based model
    Young Han Kim
    [J]. Korean Journal of Chemical Engineering, 2014, 31 : 944 - 948
  • [5] Sequential simulation of packed distillation columns using rate-based model
    Kim, Young Han
    [J]. KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2014, 31 (06) : 944 - 948
  • [6] Simulation of ternary distillation in a heat integrated distillation column (HIDiC) with a rate-based model
    Matsuda, Keigo
    Huang, Kejin
    Nakaiwa, Masaru
    Ohmori, Takao
    Endo, Akira
    Yamamoto, Takuji
    Kataoka, Sho
    Iwakabe, Koichi
    Nakanishi, Toshinari
    Kataoka, Kunio
    Takamatsu, Takeichiro
    [J]. JOURNAL OF THE CHINESE INSTITUTE OF CHEMICAL ENGINEERS, 2006, 37 (05): : 467 - 474
  • [7] Reactive distillation in a dividing wall column: Rate-based modeling and simulation
    Mueller, Ivo
    Kenig, Eugeny Y.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (11) : 3709 - 3719
  • [8] Analysis of packed distillation columns with a rate-based model
    Lee, YS
    Kim, MG
    Ha, DM
    Oda, A
    Ito, C
    Aragaki, T
    Mori, H
    [J]. KOREAN JOURNAL OF CHEMICAL ENGINEERING, 1997, 14 (05) : 321 - 324
  • [9] Analysis of packed distillation columns with a rate-based model
    Young Sei Lee
    Moon Gab Kim
    Dong Myeong Ha
    Akiyoshi Oda
    Chikara Ito
    Tsutomu Aragaki
    Hideki Mori
    [J]. Korean Journal of Chemical Engineering, 1997, 14 : 321 - 324
  • [10] Development of a mass transfer model for the rate-based simulation of a batch distillation column
    Margarita May-Vazquez, Mayra
    Alberto Rodriguez-Angeles, Mario
    Israel Gomez-Castro, Fernando
    Espinoza-Zamora, Jesus
    Murrieta-Luna, Edilberto
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2020, 140
12345