Scale-up of Bubble Column Reactors: A Review of Current State-of-the-Art

被引:86
|
作者
Shaikh, Ashfaq [1 ]
Al-Dahhan, Muthanna [2 ]
机构
[1] Eastman Chem Co, Eastman Res Div, Kingsport, TN 37662 USA
[2] Missouri Univ Sci & Technol, Rolla, MO 65409 USA
关键词
GAS HOLDUP; MASS-TRANSFER; SLURRY REACTOR; FLOW REGIME; PRESSURE; HYDRODYNAMICS; SIMULATION; STRATEGY; DESIGN; DISENGAGEMENT;
D O I
10.1021/ie302080m
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In multiphase flow reaction systems, in general, an extrapolation of small diameter behavior to larger ones is always an important and challenging task. The critical issue in such an extrapolation remains to be mixing and hydrodynamic characteristics. It needs reliable similarity criteria that would result in similar mixing and hydrodynamics and hence transport and performance in two different scales. Numerous experimental and computational studies have been performed to investigate the flow behavior of bubble column reactors for a proper design and scale-up. Experimental techniques vary from simple visual observation to more advanced noninvasive diagnostic techniques. On computational front the progress has been made from simple reactor models to fundamentally based Computational Fluid Dynamics (CFD). Such studies ultimately provide a knowledge that help in understanding the hydrodynamic and mixing characteristics of these reactors and would aid in its scale-up. Based on these studies, various methodologies have been proposed in literature for scale-up and/or to maintain their hydrodynamic and mixing similarity. This article attempts to review the current state of reported dynamic similarity and scale-up methods of bubble column reactors. It mostly covers the methods reported in open literature. The scale-up practices in industry appear to be proprietary for obvious reasons.
引用
收藏
页码:8091 / 8108
页数:18
相关论文
共 50 条
  • [31] Engineering scale-up of the bubble column slurry reactor for Fischer-Tropsch synthesis
    Zhao, Yulong
    Huaxue Fanying Gongcheng Yu Gongyi/Chemical Reaction Engineering and Technology, 2008, 24 (05): : 461 - 467
  • [32] On steady state multiplicity in bubble column reactors
    Shaikh, A.A.
    Varma, A.
    Chemical engineering journal, 1988, 39 (03): : 191 - 195
  • [33] Review of Major Design and Scale-up Considerations for Solar Photocatalytic Reactors
    Braham, Rowan J.
    Harris, Andrew T.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (19) : 8890 - 8905
  • [34] Scale-up cultivation of Chlorella ellipsoidea from indoor to outdoor in bubble column bioreactors
    Wang, Shi-Kai
    Hu, Yi-Ru
    Wang, Feng
    Stiles, Amanda R.
    Liu, Chun-Zhao
    BIORESOURCE TECHNOLOGY, 2014, 156 : 117 - 122
  • [35] The art of rapid scale-up
    Laue, Klaus
    CHIMICA OGGI-CHEMISTRY TODAY, 2015, 33 (03) : 2 - 2
  • [36] FLOTATION COLUMN SCALE-UP AND MODELING
    DOBBY, GS
    FINCH, JA
    CIM BULLETIN, 1986, 79 (889): : 89 - 96
  • [38] A scale-up strategy for a commercial scale bubble column slurry reactor for Fischer-Tropsch synthesis
    Krishna, R
    OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES, 2000, 55 (04): : 359 - 393
  • [39] State-of-the-art in the monolithic catalysts/reactors
    Tomasic, Vesna
    Jovic, Franjo
    APPLIED CATALYSIS A-GENERAL, 2006, 311 : 112 - 121
  • [40] State-of-the-Art in Zeolite Membrane Reactors
    J. Coronas
    J. Santamaria
    Topics in Catalysis, 2004, 29 : 29 - 44