An Experimental Investigation of Ducted, Reactive, Turbulent Jet Mixing with Recirculation

1977 ◽  
Author(s):  
D. E. Chriss
2002 ◽  
Vol 972 (1) ◽  
pp. 254-259 ◽  
Author(s):  
HUI HU ◽  
TETSUO SAGA ◽  
TOSHIO KOBAYASHI ◽  
NOBUYUKI TANIGUCHI

2020 ◽  
Vol 8 (6) ◽  
pp. 5038-5041

The demand for better quality drinking water gives inspiration for advancement in the functioning of water treatment processes. Jet mixing technology, widely adopted in Flocculation process is unique due to its advantages over mechanical stirrer or vanes. Jet flocculator take primacy, as it do not have any moving parts inside the reactor. The present experimental investigation focuses on the examination of jets in flocculation. Comprehensive study of various parameters such as nozzle diameter, angle of inclination, flow pattern and jet position in two geometrical shapes of flocculation chamber: Square and Circular. Effect of tank shapes on flocculation process is analysed and compared.


AIAA Journal ◽  
1982 ◽  
Vol 20 (4) ◽  
pp. 488-495
Author(s):  
W. Tabakoff ◽  
J. H. Blasenak

2001 ◽  
Vol 29 (6) ◽  
pp. 345-368 ◽  
Author(s):  
A Hilgers ◽  
B J Boersma
Keyword(s):  

1976 ◽  
Vol 43 (3) ◽  
pp. 387-395 ◽  
Author(s):  
W. L. Chow ◽  
D. J. Spring

A flow model has been devised to deal with the viscid-inviscid interaction of a class of two-dimensional incompressible separated flow problems. It is suggested that the corresponding inviscid flow of these problems is described by the free streamline theory with few unspecified parameters and their values are, in turn, determined by the viscous flow considerations. The problem of a flow past a backward facing step is selected for study in detail. The viscous flow components of turbulent jet mixing, recompression, and reattachment are delineated and studied individually. When they are later combined, it is found that the point of reattachment behaves as a saddle-point-type singularity in the system of differential equations describing the viscous flow process. This feature is employed to the determination of the aforementioned free parameters and thus the establishment of the overall corresponding inviscid flow field. The resulting base pressure coefficient for the specific case agrees reasonably well with the available experimental data. Additional calculations are performed to demonstrate the influence of higher Reynolds numbers and the values of the similarity (or spread rate) parameter σ of the “constant pressure” turbulent jet mixing process. Further studies of redevelopment of the viscous flow after reattachment, the turbulent exchange within the recompression and redevelopment regions, and the effect of wind tunnel-wall interference on the overall flow patterns have been suggested and discussed.


Sign in / Sign up

Export Citation Format

Share Document