Performance analysis and modeling of catalytic trickle-bed reactors: a comprehensive review

被引:12
|
作者
Azarpour, Abbas [1 ]
Rezaei, Nima [1 ,2 ]
Zendehboudi, Sohrab [1 ]
机构
[1] Mem Univ, Fac Engn & Appl Sci, St John, NF, Canada
[2] Lappeenranta Lahti Univ Technol, Dept Separat Sci, Lappeenranta, Finland
基金
加拿大自然科学与工程研究理事会;
关键词
Trickle-bed reactor; Hydrodynamic; Catalyst; Modeling; Design; Review; INTERFACIAL MASS-TRANSFER; VAPOR-LIQUID-EQUILIBRIUM; WET AIR OXIDATION; FISCHER-TROPSCH CATALYSTS; HENRYS LAW CONSTANT; PRESSURE-DROP; WETTING EFFICIENCY; POROUS-MEDIA; PACKED-BEDS; HYDRODYNAMIC PARAMETERS;
D O I
10.1016/j.jiec.2021.04.020
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Trickle-bed reactors (TBRs) are extensively used in industry. There have been great progresses in design and control of the TBRs. However, more improvements are required in the performance/operation of TBRs. These improvements can lead to more efficient process control and further reduction of the operation costs. In terms of process efficiency, the product quality can be improved since a large number of the TBRs are used in purification processes. In terms of operation costs, the process improvement can result in longer utilization of the catalysts because the catalytic TBRs' operations usually suffer from the deactivation phenomenon for expensive catalysts. Hydrodynamic parameters play significant roles in the control and operation of TBRs. We provide comprehensive information and discussion on TBRs application and hydrodynamic characteristics. Moreover, a systematic methodology is proposed to develop a TBR mathematical model. A detailed review on the previous TBRs studies is presented, and technical issues in their design and operation are discussed. In addition, current challenges in the TBR modeling are summarized, and further research plans/topics are suggested. This review provides an exhaustive knowledge and practical and theoretical tips that can be employed to more efficaciously model targeted TBR processes, leading to better understanding of the process behaviours, and more efficient operation of the relevant plants. (c) 2021 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 41
页数:41
相关论文
共 50 条
  • [31] TRICKLE-BED REACTORS WITH SOLID-BED CATALYSTS
    不详
    [J]. CHEMIE INGENIEUR TECHNIK, 1978, 50 (06) : 483 - 484
  • [32] Mass transfer intensification in trickle-bed reactors
    Gancarczyk, Anna
    Bartelmus, Grazyna
    Szczotka, Anna
    [J]. PRZEMYSL CHEMICZNY, 2012, 91 (11): : 2248 - 2252
  • [33] HEAT-TRANSFER IN TRICKLE-BED REACTORS
    SPECCHIA, V
    BALDI, G
    [J]. CHEMICAL ENGINEERING COMMUNICATIONS, 1979, 3 (06) : 483 - 499
  • [34] Investigations of periodically operated trickle-bed reactors
    Lange, R.
    Hanika, J.
    Stradiotto, D.
    Hudgins, R. R.
    Silveston, P. L.
    [J]. CHEMICAL ENGINEERING SCIENCE, 1994, 49 (24B) : 5615 - 5621
  • [35] GLOBAL VERSUS INTRINSIC KINETICS IN MODELING TRICKLE-BED HYDROTREATMENT REACTORS
    JONES, R
    PENDERGAST, T
    SEAPAN, M
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1984, 188 (AUG): : 44 - INDE
  • [36] Modeling and comparison of acetophenone hydrogenation in trickle-bed and slurry airlift reactors
    Bergault, I
    Rajashekharam, MV
    Chaudhari, RV
    Schweich, D
    Delmas, H
    [J]. CHEMICAL ENGINEERING SCIENCE, 1997, 52 (21-22) : 4033 - 4043
  • [37] Liquid and gas distribution in trickle-bed reactors
    Moller, LB
    Halken, C
    Hansen, JA
    Bartholdy, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (03) : 926 - 930
  • [38] Catalyst wetting characteristics in trickle-bed reactors
    Kundu, A
    Nigam, KDP
    Verma, RP
    [J]. AICHE JOURNAL, 2003, 49 (09) : 2253 - 2263
  • [39] LIQUID HOLDUP AND DISPERSION IN TRICKLE-BED REACTORS
    SCHWARTZ, JG
    WEGER, E
    DUDUKOVIC, MP
    [J]. AICHE JOURNAL, 1976, 22 (05) : 953 - 956
  • [40] HdPro: a mathematical model of trickle-bed reactors for the catalytic hydroprocessing of oil feedstocks
    Avraam, DG
    Vasalos, LA
    [J]. CATALYSIS TODAY, 2003, 79 (1-4) : 275 - 283