Maximum stable bubble size and gas holdup in high-pressure slurry bubble columns

被引:186
作者
Luo, XK [1 ]
Lee, DJ [1 ]
Lau, R [1 ]
Yang, GQ [1 ]
Fan, LS [1 ]
机构
[1] Ohio State Univ, Dept Chem Engn, Columbus, OH 43210 USA
关键词
D O I
10.1002/aic.690450402
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experiments of pressure effects on gas holdup and bubble size in slurry bubble columns at 5.6 MPa and at gas velocities up to 45 cm/s indicate that the gas holdup increases with ail increase in pressure especially at high slurry concentration. At ambient pressure, a higher solids concentration significantly lowers gas holdup over rite entire gas-velocity range, while at 5.6 MPa, the effect of solids concentration on gas holdup is relatively small at gas velocities above 25 cm/s. Ail empirical correlation was developed based on these data and those in the literature to predict gas holdup in bubble and slurry bubble columns over a wide range of operating conditions. An analysis Of bubble flow characteristics during dynamic gas disengagement indicates that large bubbles play a key role in determining gas holdup due to the large bubble and wake volumes that induce the acceleration Of small bubbles. Direct measurements of bubble size shows that elevated pressures lead to smaller bubble size and narrower bubble-size distributions. Bubble size increases significantly with increasing solids concentration at ambient pressure, while at high pressures this effect is less pronounced. A theoretical analysis of circulation of gas inside die bubble yields an analytical expression for maximum stable bubble size in high-pressure slurry bubble columns. Based on this internal circulation model, the maximum stable bubble size at high pressures is significantly smaller due to the high gas inertia and low, gas-liquid surface tension. The smaller bubble size and its reduced bubble rise velocity account for the observed pressure effect on gas holdup.
引用
收藏
页码:665 / 680
页数:16
相关论文
共 57 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]  
Bach H., 1978, GER CHEM ENG, V1, P270
[3]   THE STABILITY OF A LARGE GAS BUBBLE RISING THROUGH LIQUID [J].
BATCHELOR, GK .
JOURNAL OF FLUID MECHANICS, 1987, 184 :399-422
[4]   EFFECTS OF SURFACE TENSION AND VISCOSITY ON TAYLOR INSTABILITY [J].
BELLMAN, R ;
PENNINGTON, RH .
QUARTERLY OF APPLIED MATHEMATICS, 1954, 12 (02) :151-162
[5]   PARTICLE IMAGE VELOCIMETRY FOR CHARACTERIZING THE FLOW STRUCTURE IN 3-DIMENSIONAL GAS-LIQUID-SOLID FLUIDIZED-BEDS [J].
CHEN, RC ;
FAN, LS .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (13-14) :3615-3622
[6]  
CHEN YM, 1988, UNPUB CRITERIA RAYLE
[7]  
Clift R, 1978, Bubbles, drops, and particles, DOI 10.1080/07373939308916817
[8]   MEASUREMENT OF GAS HOLDUPS AND SAUTER MEAN BUBBLE DIAMETERS IN BUBBLE COLUMN REACTORS BY DYNAMIC GAS DISENGAGEMENT METHOD [J].
DALY, JG ;
PATEL, SA ;
BUKUR, DB .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (13-14) :3647-3654
[9]  
Deckwer W. D., 1992, BUBBLE COLUMN REACTO
[10]   IMPROVED TOOLS FOR BUBBLE COLUMN REACTOR DESIGN AND SCALE-UP [J].
DECKWER, WD ;
SCHUMPE, A .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (05) :889-911