Research on the Flow Pattern of Bubble Plume in an Aeration Tank

2010 ◽  
Author(s):  
W. H. Liu ◽  
T. Wan ◽  
W. Cheng ◽  
Yuichi Murai ◽  
Liejin Guo ◽  
...  
2010 ◽  
Vol 61 (2) ◽  
pp. 407-414 ◽  
Author(s):  
M. Gresch ◽  
D. Braun ◽  
W. Gujer

Reactor hydraulics is one of the key factors for plant performance and plant control. The residence time distribution is a good but limited indicator of reactor hydraulics. A more detailed view is obtained by direct observations within the reactor. Two different techniques (conservative tracer, reactive tracer) are discussed to detect major anomalies in the flow field of a wastewater aeration tank. Experiments with conservative tracers give valuable information over a very limited period of time making the analysis of the flow field difficult. On the other hand, reactive tracers can be monitored long term which helps identifying the flow pattern provided that a high spatial and temporal resolution of the measurements is applied. Experimental data is used to determine the structure and the parameters of a compartment model that corresponds well with the measurements.


2020 ◽  
Vol 71 (6) ◽  
pp. 408-417
Author(s):  
Wan Tian ◽  
Yan Xingxing ◽  
Cheng Wen ◽  
Ren Jiehui ◽  
Wang Min ◽  
...  

Aeration is crucial for biological wastewater treatment process but energy intensive. Aerated pore distribution in an aeration tank can control oxygen transfer and energy consumption. Therefore, this study aimed at elucidating the fundamental flow structure of gas phase in bubble plumes in a cylindrical tank with different aerated pore distance (ranged from 0.03-0.09m). Both experiments and numerical simulation were used. PIV (Particle Image velocimetry) technology was used for getting bubble phase flow field. Bubble population behavior model (BPBM) coupled with computational fluid dynamics (CFD) was established for numerical simulation. Results showed that aeration distances greatly affected the movement of gas-phase. When the aeration distances were large or small, the attractive interaction generated by air columns in different aeration pore caused a turbulence of bubble plume. At the meanwhile, a large of bubbles separated from the main air columns, which resulted in an unsteady gas-phase structure. The structure of bubble plume was relatively stable with an aerator spacing of 0.0625m in this study, which was beneficial for the connection between gas-phase and liquid-phase.


Author(s):  
Y. Pan

The D defect, which causes the degradation of gate oxide integrities (GOI), can be revealed by Secco etching as flow pattern defect (FPD) in both float zone (FZ) and Czochralski (Cz) silicon crystal or as crystal originated particles (COP) by a multiple-step SC-1 cleaning process. By decreasing the crystal growth rate or high temperature annealing, the FPD density can be reduced, while the D defectsize increased. During the etching, the FPD surface density and etch pit size (FPD #1) increased withthe etch depth, while the wedge shaped contours do not change their positions and curvatures (FIG.l).In this paper, with atomic force microscopy (AFM), a simple model for FPD morphology by non-crystallographic preferential etching, such as Secco etching, was established.One sample wafer (FPD #2) was Secco etched with surface removed by 4 μm (FIG.2). The cross section view shows the FPD has a circular saucer pit and the wedge contours are actually the side surfaces of a terrace structure with very small slopes. Note that the scale in z direction is purposely enhanced in the AFM images. The pit dimensions are listed in TABLE 1.


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