Mass transfer coefficients in mechanically agitated gas-liquid contactors

被引:26
作者
Markopoulos, Joannis [1 ]
Christofi, Chrystalla [1 ]
Katsinaris, Ioannis [1 ]
机构
[1] Aristotle Univ Thessaloniki, Dept Chem Engn, GR-54124 Thessaloniki, Greece
关键词
agitation; gas-liquid systems; mass transfer; Newtonian fluids;
D O I
10.1002/ceat.200600394
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
There are a large number of correlations given in literature for the prediction of volume-related liquid-side mass transfer coefficients in mechanically agitated gas-liquid contactors. Significant disagreement can be observed concerning the proposed correlations, so that no single correlation exists representing all of the mass transfer data given in the literature. The observed differences can mainly be ascribed to the differences in the geometry of the system, the range of operational conditions and the measurement method used. On the basis of a comparative study of mass transfer phenomena in agitated Newtonian and non-Newtonian aerated liquids, a critical discussion of the literature results is presented in this review article, so that final conclusions can be drawn for the k(L)a values in the different single- and multiple-impeller agitated systems studied in the literature.
引用
收藏
页码:829 / 834
页数:6
相关论文
共 53 条
[1]   Gas-liquid mass transfer in dual impeller bioreactor [J].
Arjunwadkar, SJ ;
Sarvanan, K ;
Kulkarni, PR ;
Pandit, AB .
BIOCHEMICAL ENGINEERING JOURNAL, 1998, 1 (02) :99-106
[2]   Bubble size and mass transfer coefficients in dual-impeller agitated reactors [J].
Bouaifi, MI ;
Roustan, M .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1998, 76 (03) :390-397
[3]  
CAGNON H, 1998, CAN J CHEM ENG, V76, P379
[4]   THE CONTINUOUS PHASE HEAT AND MASS-TRANSFER PROPERTIES OF DISPERSIONS [J].
CALDERBANK, PH ;
MOOYOUNG, MB .
CHEMICAL ENGINEERING SCIENCE, 1961, 16 (1-2) :39-54
[5]  
CHANDRASEKHARAN K, 1981, CHEM ENG SCI, V36, P819
[6]   Comparison of mass transfer performance for various single and twin impellers [J].
Chen, ZD ;
Chen, JJJ .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 1999, 77 (A2) :104-109
[7]   Performance of agitated gas-liquid contactors [J].
Cooper, CM ;
Fernstrom, GA ;
Miller, SA .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1944, 36 :504-509
[8]  
DAVIES SM, 1985, P 5 EUR C MIX BHRA W
[9]   ON THE METHODS FOR THE DETERMINATION OF THE OXYGEN-TRANSFER COEFFICIENT IN MECHANICALLY AGITATED VESSELS [J].
DENIS, A ;
THIBAULT, J ;
LEDUY, A .
CHEMICAL ENGINEERING COMMUNICATIONS, 1990, 94 :35-51
[10]  
FIGUEIREDO MM, 1979, CHEM ENG SCI, V34, P1333