Bubble columns with fine pore sparger operating in the pseudo-homogeneous regime: Gas hold up prediction and a criterion for the transition to the heterogeneous regime

被引:64
作者
Kazakis, N. A. [1 ]
Papadopoulos, I. D. [1 ]
Mouza, A. A. [1 ]
机构
[1] Aristotle Univ Thessaloniki, Dept Chem Engn, GR-54124 Thessaloniki, Greece
关键词
bubble columns; porous sparger; pseudo-homogeneous regime; gas holdup; liquid properties; transition point;
D O I
10.1016/j.ces.2007.03.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
New experimental data concerning the gas holdup in bubble columns equipped with porous sparger were acquired. The effect of liquid properties and sparger characteristic (i.e., pore size, dimensions) on gas holdup at the pseudo-homogeneous regime has been studied and a correlation regarding the prediction of the transition point from the pseudo-homogeneous to the heterogeneous regime has been proposed and found to be in good agreement with available data. Moreover, a previously proposed correlation [Mouza, A.A., Dalakoglou, G.K., Paras, S.V., 2005. Effect of liquid properties on the performance of bubble column reactors with fine pore spargers. Chemical Engineering Science 60(5), 1465-1475], for the prediction of gas holdup at the homogeneous regime for this type of equipment, has been modified to take into account the effect of the mean pore diameter and it is also found to be in good agreement with published data. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3092 / 3103
页数:12
相关论文
共 24 条
[1]   GAS HOLDUP AND VOLUMETRIC MASS-TRANSFER COEFFICIENT IN BUBBLE COLUMNS - EFFECTS OF LIQUID PROPERTIES [J].
AKITA, K ;
YOSHIDA, F .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (01) :76-80
[2]   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
[3]   A generalized approach to model oxygen transfer in bioreactors using population balances and computational fluid dynamics [J].
Dhanasekharan, KM ;
Sanyal, J ;
Jain, A ;
Haidari, A .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (01) :213-218
[4]  
Hebrard G, 1996, CHEM ENG RES DES, V74, P406
[5]   GAS HOLD-UP IN BUBBLE-COLUMNS [J].
HIKITA, H ;
ASAI, S ;
TANIGAWA, K ;
SEGAWA, K ;
KITAO, M .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1980, 20 (01) :59-67
[6]   MECHANISM OF FORMATION OF GAS BUBBLE-BEDS [J].
HOUGHTON, G ;
MCLEAN, AM ;
RITCHIE, PD .
CHEMICAL ENGINEERING SCIENCE, 1957, 7 (1-2) :40-&
[7]   HOLDUP AND MASS TRANSFER IN BUBBLE COLUMNS [J].
HUGHMARK, GA .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1967, 6 (02) :218-&
[8]  
Jones Timothy J, 2002, J Extra Corpor Technol, V34, P34
[9]   Coherent flow structures in bubble column reactors [J].
Joshi, JB ;
Vitankar, VS ;
Kulkarni, AA ;
Dhotre, MT ;
Ekambara, K .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (16) :3157-3183
[10]  
Kaji M., 2001, P 5 WORLD C EXP HEAT, P1503