The axial dispersion of liquid solutions and solid suspensions in planar oscillatory flow crystallizers

AIChE Journal ◽  
2019 ◽  
Vol 65 (9) ◽  
Author(s):  
Patrícia Cruz ◽  
Carolina Silva ◽  
Fernando Rocha ◽  
António Ferreira
2021 ◽  
Vol 60 (6) ◽  
pp. 2663-2676
Author(s):  
Patrícia C. Cruz ◽  
Carolina R. Silva ◽  
Fernando A. Rocha ◽  
António M. Ferreira

1994 ◽  
Vol 60 (579) ◽  
pp. 3672-3679
Author(s):  
Gaku Tanaka ◽  
Yoshiro Ueda ◽  
Hideki Fujioka ◽  
Kazuo Tanishita

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

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

1998 ◽  
Vol 120 (3) ◽  
pp. 405-415 ◽  
Author(s):  
G. Tanaka ◽  
Y. Ueda ◽  
K. Tanishita

The efficiency of axial gas dispersion during ventilation with high-frequency oscillation (HFO) is improved by manipulating the oscillatory flow waveform such that intermittent oscillatory flow occurs. We therefore measured the velocity profiles and effective axial gas diffusivity during intermittent oscillatory flow in a straight tube to verify the intermittency augmentation effect on axial gas transfer. The effective diffusivity was dependent on the flow patterns and significantly increased with an increase in the duration of the stationary phase. It was also found that the ratio of effective diffusivity to molecular diffusivity is two times greater than that in sinusoidal oscillatory flow. Moreover, turbulence during deceleration or at the beginning of the stationary phase further augments axial dispersion, with the effective diffusivity being over three times as large, thereby proving that the use of intermittent oscillatory flow effectively augments axial dispersion for ventilation with HFO.


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