Particle-liquid mass transfer coefficient in two-/three-phase stirred tank reactors

被引:79
作者
Pangarkar, VG [1 ]
Yawalkar, AA
Sharma, MM
Beenackers, AACM
机构
[1] Univ Inst Chem Technol, Dept Chem Engn, Bombay 400019, Maharashtra, India
[2] Univ Groningen, Dept Chem Engn, NL-9747 AG Groningen, Netherlands
关键词
D O I
10.1021/ie010933j
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Knowledge of particle-liquid mass transfer coefficient. (k(SL)) is important for a rational design of a solid-liquid/solid-liquid-gas stirred tank reactor (STR). Considerable efforts have been made by different investigators to study and Correlate the behavior of k(SL) in STRs for a variety of geometric and operating conditions. This review attempts to put together and analyze the information available in the literature on k(SL) in STRs systematically. Different approaches,used by researchers to correlate k(SL) are critically. discussed. The effect of system configurations (type of the impeller, D/T, and C/T), operating parameters, (impeller speed/power input, particle loading, and gas flow rate), and physical properties (d(P), D-m, mu, and Deltarho), on k(SL), have been discussed elaborately. Some new data for six-bladed impellers have been generated to determine the optimum geometric configuration and operating conditions for particle-liquid mass transfer in three-phase STRs. It is concluded that k(SL) in two-/three-phase STRs can be correlated reliably over a wide range of system configurations and operating:parameters, by a relative, particle suspension term, N/N-S(G). Scope and need for further studies. have been suggested.
引用
收藏
页码:4141 / 4167
页数:27
相关论文
共 130 条
[1]   DETERMINATION OF THE MINIMUM AGITATION SPEED TO ATTAIN THE JUST DISPERSED STATE IN SOLID-LIQUID AND LIQUID-LIQUID REACTORS PROVIDED WITH MULTIPLE IMPELLERS [J].
ARMENANTE, PM ;
HUANG, YT ;
LI, T .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (9-11) :2865-2870
[2]  
ARMENANTE PM, 1989, CHEM ENG SCI, V44, P2701
[3]   EFFECT OF SPARGED GAS ON MASS-TRANSFER BETWEEN FINE PARTICLES AND LIQUIDS IN AN AGITATED VESSEL [J].
ASAI, S ;
KONISHI, Y ;
KAJIWARA, T .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1989, 22 (01) :96-98
[4]   MASS-TRANSFER BETWEEN FINE PARTICLES AND LIQUIDS IN AGITATED VESSELS [J].
ASAI, S ;
KONISHI, Y ;
SASAKI, Y .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1988, 21 (02) :107-112
[5]  
Aussenac D, 1982, P 4 EUR C MIX NOORDW, P417
[6]   COMPLETE SUSPENSION OF PARTICLES IN MECHANICALLY AGITATED VESSELS [J].
BALDI, G ;
CONTI, R ;
ALARIA, E .
CHEMICAL ENGINEERING SCIENCE, 1978, 33 (01) :21-25
[7]   MASS TRANSFER COEFFICIENTS FOR SOLIDS SUSPENDED IN AGITATED LIQUIDS [J].
BARKER, JJ ;
TREYBAL, RE .
AICHE JOURNAL, 1960, 6 (02) :289-295
[8]  
BATCHELOR CK, 1980, J FLUID MECH, V98, P609
[9]  
BEENACKERS AAC, 1986, CHEM REACTOR DESIGN, P463
[10]  
BENETT CO, 1962, MOMENTIUM HEAT MASS