scholarly journals Numerical Analysis of Axial Dispersion in an Intermittent Oscillatory Flow.

1993 ◽  
Vol 59 (566) ◽  
pp. 3078-3085 ◽  
Author(s):  
Hideki Fujioka ◽  
Gaku Tanaka ◽  
Masahiro Nishida ◽  
Kazuo Tanishita
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

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

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.


2005 ◽  
Vol 60 (1) ◽  
pp. 111-122 ◽  
Author(s):  
B.D. Crittenden ◽  
A. Lau ◽  
T. Brinkmann ◽  
R.W. Field

1987 ◽  
Vol 32 (2) ◽  
pp. 277-282 ◽  
Author(s):  
R.W. Yeo ◽  
T.Z. Fahidy

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