Effects of liquid property on gas holdup and mass transfer in co-current downflow contacting column

被引:14
作者
Akosman, C [1 ]
Orhan, R [1 ]
Dursun, G [1 ]
机构
[1] Firat Univ, Dept Chem Engn, TR-23279 Elazig, Turkey
关键词
gas holdup; mass transfer; k(L)a; CDCC; liquid property; correlation;
D O I
10.1016/j.cep.2003.09.004
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The effects of liquid property on gas holdup and mass transfer in a co-current downflow contacting column (CDCC) were investigated using air-aqueous glycerol (Analar Reagent, Merck) solutions (AG) with changing the concentration up to 1.5% (w/w). The experiments were conducted using various nozzle diameters at different superficial gas velocities and liquid re-circulation rates. Gas holdup and liquid-side mass transfer coefficient increased with increasing superficial gas velocity and liquid flow rate but decreased with increasing glycerol concentration. The values of gas holdup and mass transfer coefficient in air-aqueous glycerol system were found to be lower than those in air-water system. New correlations for the estimation of gas holdup and mass transfer coefficient in CDCC are proposed. These proposed correlations in terms of liquid kinetic power per liquid volume in the column, superficial gas velocity and relative surface tension fit the experimental data of gas holdup and mass transfer coefficient reasonably well for all gas and liquid flow rates and nozzle diameters used. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:503 / 509
页数:7
相关论文
共 35 条
[1]   BUBBLE SIZE, INTERFACIAL AREA, AND LIQUID-PHASE MASS-TRANSFER COEFFICIENT IN BUBBLE COLUMNS [J].
AKITA, K ;
YOSHIDA, F .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1974, 13 (01) :84-91
[2]   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
[3]  
[Anonymous], 1984, GER CHEM ENG
[4]   MASS-TRANSFER OF GAS-BUBBLES UNDER THE INFLUENCE OF SURFACTANTS [J].
BISCHOF, F ;
SOMMERFELD, M ;
DURST, F .
CHEMIE INGENIEUR TECHNIK, 1993, 65 (11) :1365-1367
[5]   THE DETERMINATION OF MASS-TRANSFER RATES FROM INDIVIDUAL SMALL BUBBLES [J].
BISCHOF, F ;
SOMMERFELD, M ;
DURST, F .
CHEMICAL ENGINEERING SCIENCE, 1991, 46 (12) :3115-3121
[6]   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
[7]  
CHABBARA RP, 1993, ENCY FLUID MECH
[8]  
Deckwer W. D., 1992, BUBBLE COLUMN REACTO
[9]   APPLICABILITY OF AXIAL-DISPERSION MODEL TO ANALYZE MASS-TRANSFER MEASUREMENTS IN BUBBLE-COLUMNS [J].
DECKWER, WD ;
NGUYENTIEN, K ;
KELKAR, BG ;
SHAH, YT .
AICHE JOURNAL, 1983, 29 (06) :915-922
[10]  
DEEKE D, 1986, CHEM ENG SCI, V49, P2273