Effects of Column Diameter on the Holdups of Bubble, Wake and Continuous Liquid Phase in Bubble Columns with Viscous Liquid Medium

被引:0
作者
Lim, Dae Ho [1 ]
Jang, Ji Hwa [1 ]
Kang, Yong [1 ]
Jun, Ki Won [2 ]
机构
[1] Chungnam Natl Univ, Sch Chem Engn, 220 Gung Dong, Daejeon 305764, South Korea
[2] Korea Res Inst Chem Technol, Green Chem Technol Div, Daejeon 305600, South Korea
来源
KOREAN CHEMICAL ENGINEERING RESEARCH | 2011年 / 49卷 / 05期
关键词
Bubble Column; Phase Holdup; Wake Phase; Viscous Liquid Media;
D O I
暂无
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Holdup characteristics of bubble, wake and continuous liquid phases were investigated in bubble columns with viscous liquid media. Effects of column diameter(0.051, 0.076, 0.102 and 0.152 m ID), gas velocity(U-G=0.02 similar to 0.16 m/s) and liquid viscosity(mu(L)=0.001 similar to 0.050 Pa.s) of continuous liquid media on the holdups of bubble, wake and continuous liquid phases were discussed. The three phase such as bubble, wake and continuous liquid phases were classified successfully by adapting the dual electrical resistivity probe method. Compressed filtered air and water or aqueous solutions of CMC(Carboxy Methyl Cellulose) were used as a gas and a liquid phase, respectively. To detect the wake as well as bubble phases in the bubble column continuously, a data acquisition system(DT 2805 Lab Card) with personal computer was used. The analog signals obtained from the probe circuit were processed to produce the digital data, from which the wake phase was detected behind the multi-bubbles as well as single bubbles rising in the bubble columns. The holdup of bubble and wake phases decreased but that of continuous liquid media increased, with an increase in the column diameter or liquid viscosity. However, the holdup of bubble and wake phases increased but that of continuous media decreased with an increase in the gas velocity. The holdup ratio of wake to wake to bubble phase decreased with an increase in the column diameter or gas velocity, however, increased with an increase in the viscosity of continuous liquid media. The holdups of bubble, wake and continuous liquid media could be correlated in terms of operating variables within this experimental conditions as: epsilon(B) = 0.043D U-0.18(G)0.56 mu(0.13)(L), epsilon(W) = 0.003D U-0.85(G)0.46 mu(0.10)(L), epsilon(C) = 1.179D U-0.09(G)0.13 mu(0.04)(L).
引用
收藏
页码:582 / 587
页数:6
相关论文
共 23 条
[1]  
Celata G. P., 2006, INT J MULTIPHASE FLO, V30, P939
[2]   Bubble wake dynamics of a single bubble rising in the freeboard of a two-dimensional liquid-solid fluidized bed [J].
Chen, RC ;
Wang, FM ;
Lin, TJ .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) :4831-4838
[3]   Wake structure of a single bubble rising in a two-dimensional column [J].
Chen, RC ;
Chou, IS .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 1998, 17 (03) :165-178
[4]  
Deckwer W.D., 1992, BUBBLE COLUMN REACTO
[5]  
FAN LS, 1990, BUBBLE DYNAMICS LIQU
[6]   Flow of non-Newtonian fluids around bubbles: PIV measurements and birefringence visualisation [J].
Funfschilling, D ;
Li, HZ .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (03) :1137-1141
[7]  
Jang JH, 2010, KOREAN CHEM ENG RES, V48, P359
[8]  
Jang JH, 2009, KOREAN CHEM ENG RES, V47, P587
[9]  
Kang Y, 2008, KOREAN CHEM ENG RES, V46, P451
[10]   Heat and mass transfer in three-phase fluidized-bed reactors - an overview [J].
Kim, SD ;
Kang, Y .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (21-22) :3639-3660