MICROMIXING IN TWO-PHASE (G-L AND S-L) SYSTEMS IN A STIRRED VESSEL

被引:19
作者
Hofinger, Julia [1 ]
Sharpe, Robert W. [1 ]
Bujalski, Waldemar [1 ]
Bakalis, Serafim [1 ]
Assirelli, Melissa [2 ]
Eaglesham, Archie [2 ]
Nienow, Alvin W. [1 ]
机构
[1] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
[2] Huntsman Polyurethanes, B-3078 Everberg, Belgium
关键词
micromixing; stirred vessel; feed position; gas sparging; solid particles; PARTICLE IMAGE VELOCIMETRY; HIGH SOLIDS CONCENTRATION; ENERGY-DISSIPATION RATES; IODATE REACTION SYSTEM; LIQUID FLOW; PARALLEL REACTIONS; RUSHTON TURBINE; TANK; SUSPENSION; EFFICIENCY;
D O I
10.1002/cjce.20494
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The literature on micromixing and local-specific energy dissipation rate, epsilon(T) (on which it depends), for two-phase systems is limited and conflicting. Here, the competitive iodide/iodate reaction scheme has been used to study the effect of particles and gas flow rate on micromixing in a Rushton turbine agitated vessel. Gassing rates up to 1.5 vvm did not show any effect on product distribution compared to the ungassed at constant mean-specific energy dissipation rate (((epsilon) over bar (T))(g) = (epsilon) over bar (T)) for a feeding near the impeller. Near the upper liquid surface, micromixing improved with increasing flow rate because it increased fluid turbulence. These results confirm the limited literature. With 500 mu m glass beads at concentrations up to 2.5 wt.%, micromixing was unaffected near the impeller and near the surface. The related literature is very unclear and it is difficult to draw any precise conclusions. At similar to 12 wt.% when cloud formation was observed, micromixing was significantly worse, especially, it is shown for the first time, in the clear layer above the cloud. The latter finding is significant for processes such as precipitation where micromixing determines the particle characteristics.
引用
收藏
页码:1029 / 1039
页数:11
相关论文
共 53 条
[1]   An extension to the incorporation model of micromixing and its use in estimating local specific energy dissipation rates [J].
Assirelli, M. ;
Wynn, E. J. W. ;
Buialski, W. ;
Eaglesham, A. ;
Nienow, A. W. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (10) :3460-3469
[2]   Intensifying micromixing in a semi-batch reactor using a Rushton turbine [J].
Assirelli, M ;
Bujalski, W ;
Eaglesham, A ;
Nienow, AW .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (8-9) :2333-2339
[3]   Study of micromixing in a stirred tank using a Rushton turbine - Comparison of feed positions and other mixing devices [J].
Assirelli, M ;
Bujalski, W ;
Eaglesham, A ;
Nienow, AW .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2002, 80 (A8) :855-863
[4]  
ASSIRELLI M, 2004, THESIS U BIRMINGHAM
[5]   THE EFFECT OF MICROMIXING ON PARALLEL REACTIONS [J].
BALDYGA, J ;
BOURNE, JR .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (04) :907-916
[6]  
Baldyga J., 1995, CHEM ENG J, V58, P183, DOI DOI 10.1016/0923-0467(95)02982-6
[7]  
Baldyga J., 1999, Turbulent mixing and chemical reactions
[8]   SOLID DISPERSION IN AN AGITATED VESSEL [J].
BARRESI, A ;
BALDI, G .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (12) :2949-2956
[9]   Experimental investigation of interaction between turbulent liquid flow and solid particles and its effects on fast reactions [J].
Barresi, AA .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (05) :807-814
[10]   Selectivity of mixing-sensitive reactions in slurry systems [J].
Barresi, AA .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (10) :1929-1933