Experimental and theoretical analysis of axial dispersion in the liquid phase in external-loop airlift reactors

2005 ◽  
Vol 60 (22) ◽  
pp. 5945-5954 ◽  
Author(s):  
Ch. Vial ◽  
S. Poncin ◽  
G. Wild ◽  
N. Midoux
1991 ◽  
Vol 56 (6) ◽  
pp. 1249-1252
Author(s):  
Marie Fialová ◽  
Ctirad Verner ◽  
Lothar Ebner

The characteristics of axial dispersion in the liquid phase were measured for two basic flow regimes in a horizontal two-phase tube reactor. The data obtained indicate that in some flow regions, axial dispersion can be quite significant.


2017 ◽  
Vol 121 ◽  
pp. 51-60 ◽  
Author(s):  
Rajesh Kumar ◽  
H.J. Pant ◽  
Sunil Goswami ◽  
V.K. Sharma ◽  
A. Dash ◽  
...  

2019 ◽  
Vol 358 ◽  
pp. 520-530 ◽  
Author(s):  
Pavel V. Markov ◽  
Igor S. Mashkovsky ◽  
Galina O. Bragina ◽  
Johan Wärnå ◽  
Evgenii Yu. Gerasimov ◽  
...  

1994 ◽  
Vol 61 (1) ◽  
pp. 49-55 ◽  
Author(s):  
Yoshinori Kawase ◽  
Naoki Omori ◽  
Masanari Tsujimura

2004 ◽  
Vol 69 (7) ◽  
pp. 581-599 ◽  
Author(s):  
Ljubisa Nikolic ◽  
Vesna Nikolic ◽  
Vlada Veljkovic ◽  
Miodrag Lazic ◽  
Dejan Skala

The influence of the gas flow rate and vibration intensity in the presence of the solid phase (polypropylene spheres) on axial mixing of the liquid phase in a three phase (gas-liquid-solid) Karr reciprocating plate column (RPC) was investigated. Assuming that the dispersionmodel of liquid flow could be used for the real situation inside the column, the dispersion coefficient of the liquid phase was determined as a function of different operating parameters. For a two-phase liquid-solid RPC the following correlation was derived: DL = 1.26(Af)1.42 UL 0.51 ?S 0.23 and a similar equation could be applied with ? 30 % confidence for the calculation of axial dispersion in the case of a three-phase RPC: DL = 1.39(Af)0.47 UL0.42UG0.03 ?S -0.26.


Sign in / Sign up

Export Citation Format

Share Document