Oscillatory flow and axial dispersion in packed beds of spheres

2005 ◽  
Vol 60 (1) ◽  
pp. 111-122 ◽  
Author(s):  
B.D. Crittenden ◽  
A. Lau ◽  
T. Brinkmann ◽  
R.W. Field
1994 ◽  
Vol 60 (579) ◽  
pp. 3672-3679
Author(s):  
Gaku Tanaka ◽  
Yoshiro Ueda ◽  
Hideki Fujioka ◽  
Kazuo Tanishita

AIChE Journal ◽  
2019 ◽  
Vol 65 (9) ◽  
Author(s):  
Patrícia Cruz ◽  
Carolina Silva ◽  
Fernando Rocha ◽  
António Ferreira

AIChE Journal ◽  
1986 ◽  
Vol 32 (1) ◽  
pp. 170-174 ◽  
Author(s):  
Bum-Jong Ahn ◽  
André Zoulalian ◽  
J. M. Smith

AIChE Journal ◽  
1966 ◽  
Vol 12 (4) ◽  
pp. 767-773 ◽  
Author(s):  
Steven F. Miller ◽  
C. Judson King

2003 ◽  
Vol 2003.2 (0) ◽  
pp. 187-188
Author(s):  
Tatsuo NISHIMURA ◽  
Takeshi KANAI ◽  
Koji KUNITSUGU

1976 ◽  
Vol 9 (4) ◽  
pp. 294-301 ◽  
Author(s):  
AKINORI MATSUURA ◽  
TAKASHI AKEHATA ◽  
TAKASHI SHIRAI
Keyword(s):  

2018 ◽  
Vol 4 (2) ◽  
pp. 1-15 ◽  
Author(s):  
F. Almeida ◽  
F. Rocha ◽  
A. Ferreira

In this research paper the residence time distribution (RTD) was monitored for a range of fluid oscillation, frequency, amplitude and flow rate in two oscillatory flow reactors (OFR) provided with 2D smooth periodic constrictions (2D-SPC) with different designs. It was studied the axial liquid dispersion using axial dispersion model and the mixing efficiency using tank-in-series model for continuous mode. Two cases, with and without fluid oscillation, were studied and determined the optimum conditions to ensure a close plug flow, an efficient mixing and a low axial liquid dispersion. The optimum operation conditions for the two 2D-SPC designs were found. Moreover, the effect of open cross-sectional area (a) on mixing and axial dispersion was also investigated. For low cross-sectional area values the mixing is higher. It was observed that fluid oscillation increases the mixing intensity even at lower flow rates, and the axial dispersion increases as the flow rate increases.


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