Impact of plenum conditions and gas-liquid distributor on bubble column hydrodynamics

被引:7
作者
Mach, Jacob [1 ]
Parisien, Valois [1 ]
Wiens, Jason [2 ]
McKnight, Craig A. [2 ]
Macchi, Arturo [1 ]
机构
[1] Univ Ottawa, Ctr Catalysis Res & Innovat, Dept Chem & Biol Engn, Ottawa, ON K1N 6N5, Canada
[2] Syncrude Canada Ltd, 9421-17 Ave, Edmonton, AB T6N 1H4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Gas-liquid distributor; Plenum conditions; Energy dissipation rate; Turbulent bubble breakup; OPTICAL PROBES; MASS-TRANSFER; FLOWS; DISPERSION; 2-PHASE;
D O I
10.1016/j.ces.2019.115296
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In an LC-Fining (TM) hydroprocessor, the orientation of the free surface in the plenum chamber and the efficiency of the internal gas-liquid separator impact the amounts of the gas and the liquid passing through individual bubble cap risers in the grid. Various gas and liquid flowrates were thus passed through a single bubble cap riser to determine resulting bubble properties. Bubble sizes correlated well with energy dissipation rate and gas-to-liquid velocity ratio to the power of -0.4 and 0.6, respectively, in agreement with theory on the turbulent breakup of dense dispersions. Bubbles were also influenced by the gas-liquid distributor geometry, where the bubble cap produced larger bubbles than a perforated plate. Finally, the size of bubbles sparged in the plenum marginally affected overall gas holdup, suggesting that a bubble cap distributor redesign should be prioritized over upstream gas introduction equipment to optimize the performance of the hydroprocessor. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:10
相关论文
共 28 条
[1]   Single and double optical probes in air-water two-phase flows:: real time signal processing and sensor performance [J].
Barrau, E ;
Rivière, N ;
Poupot, C ;
Cartellier, A .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1999, 25 (02) :229-256
[2]   The prediction of dispersed flows boundaries in liquid-liquid and gas-liquid systems [J].
Brauner, N .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2001, 27 (05) :885-910
[3]   Influence of coalescence behaviour of the liquid and of gas sparging on hydrodynamics and bubble characteristics in a bubble column [J].
Camarasa, E ;
Vial, C ;
Poncin, S ;
Wild, G ;
Midoux, N ;
Bouillard, J .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1999, 38 (4-6) :329-344
[4]  
Cartellier A, 2001, CHEM ENG TECHNOL, V24, P535, DOI 10.1002/1521-4125(200105)24:5<535::AID-CEAT535>3.0.CO
[5]  
2-X
[6]   Mass transfer in bubble column for industrial conditions - effects of organic medium, gas and liquid flow rates and column design [J].
Chaumat, H ;
Billet-Duquenne, AM ;
Augier, F ;
Mathieu, C ;
Delmas, H .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (22) :5930-5936
[7]  
Colvert J. H., 1989, U. S. Patent, Patent No. [4,874,583, 4874583]
[8]  
Deen N., 2010, Ullmann's Encyclopedia of Industrial Chemistry
[9]   Effects of sparger height and orifice orientation on solids dispersion in a slurry bubble column [J].
Gandhi, B ;
Prakash, A ;
Bergougnou, MA .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02) :383-391
[10]   THE DESIGN OF DISTRIBUTORS FOR GAS-FLUIDIZED BEDS [J].
GELDART, D ;
BAEYENS, J .
POWDER TECHNOLOGY, 1985, 42 (01) :67-78