Suspension of solid particles in multi-impeller three-phase stirred tank reactors

被引:25
作者
Dohi, N
Matsuda, Y
Itano, N
Minekawa, K
Takahashi, T
Kawase, Y [1 ]
机构
[1] Mitsubishi Chem Corp, Ctr Res Dev & Engn, Mizushima Plant, Okayama 7128054, Japan
[2] Toyo Univ, Dept Appl Chem, Kawagoe, Saitama 3508585, Japan
关键词
solid suspension; stirred tank reactor; three-phase system; multi-impeller;
D O I
10.1002/cjce.5450790116
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Solids suspension characteristics in gas-liquid-solid three-phase stirred tanks with multi-impellers were experimentally examined. Minimum impeller speeds for ultimately homogeneous solid suspension have been measured stirred tank reactors. Three impellers were installed: two four-pitched blade downflow disk turbines and one Pfaudler type impeller chosen to provide good gas dispersion and to accomplish off-bottom suspension of solid particles, respectively. Cas dispersion causes an increase in particle sedimentation associated with a decrease in power consumption and as a result, minimum impeller speeds for ultimately homogeneous solid suspension increase with increasing gas flow rates. A correlation was developed to predict minimum impeller speeds for ultimately homogeneous solid suspension. The proposed correlation, which agrees satisfactorily with the experimental results, is expected to be useful in design and scale-up.
引用
收藏
页码:107 / 111
页数:5
相关论文
共 15 条
[1]   EXPERIMENTAL-DETERMINATION OF THE MINIMUM AGITATION SPEED FOR COMPLETE LIQUID LIQUID DISPERSION IN MECHANICALLY AGITATED VESSELS [J].
ARMENANTE, PM ;
HUANG, YT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1992, 31 (05) :1398-1406
[2]  
Bourne J.R., 1974, Chem. Eng. J, V8, P243, DOI 10.1016/0300-9467(74)85030-6
[3]  
BRUCATO A, 1991, CHEM ENG RES DES, V69, P43
[4]   PARTICLE SUSPENSION AND MASS-TRANSFER RATES IN AGITATED VESSELS [J].
DAVIES, JT .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1986, 20 (04) :175-181
[5]   Mixing characteristics in slurry stirred tank reactors with multiple impellers [J].
Dohi, N ;
Matsuda, Y ;
Itano, N ;
Shimizu, K ;
Minekawa, K ;
Kawase, Y .
CHEMICAL ENGINEERING COMMUNICATIONS, 1999, 171 :211-229
[6]   CRITICAL IMPELLER SPEED FOR SOLID SUSPENSION IN MULTI-IMPELLER 3-PHASE AGITATED CONTACTORS [J].
DUTTA, NN ;
PANGARKAR, VG .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1995, 73 (03) :273-283
[7]  
FAJNER D, 1985, CHEM ENG RES DES, V63, P235
[8]  
Harnby N., 1985, MIXING PROCESS IND
[9]   Cloud height in solids suspension agitation [J].
Hicks, MT ;
Myers, KJ ;
Bakker, A .
CHEMICAL ENGINEERING COMMUNICATIONS, 1997, 160 :137-155
[10]  
KUNII D, 1996, FLUIDIZATION ENG